JP4885141B2 - Hydrogen generation and energy generation assembly - Google Patents

Description

This application claims priority to US Provisional Patent Application Nos. 60 / 3,894 and 60 / 717,641, the entire disclosures of which are incorporated herein by reference in their entirety. .
The present disclosure is generally directed to a hydrogen generation assembly, its components, and an energy generation assembly.

A hydrogen production assembly is an assembly that converts one or more feeds into a product stream containing hydrogen gas as a major component. This feedstock includes a carbon-containing feedstock and may optionally contain water. This feed is transported from the feed transport system to the hydrogen generation zone of the hydrogen generation assembly by the feed being transported, generally under pressure and at elevated temperatures. The hydrogen production region is often associated with a temperature adjustment assembly (eg, a heating assembly or a cooling assembly). The assembly then consumes one or more fuel streams to maintain the hydrogen production region in the proper temperature range to effectively produce hydrogen gas.

  The generated hydrogen gas can be used in various applications. Such an application is for example energy generation in electrochemical fuel cells. An electrochemical fuel cell is a device that converts fuel and oxidant into electricity, reaction products and heat. For example, fuel cells can convert hydrogen and oxygen into water and electricity. In this type of fuel cell, hydrogen is the fuel, oxygen is the oxidant, and water is the reaction product. A fuel cell stack may include a plurality of fuel cells and be utilized by a hydrogen generation assembly to provide an energy generation assembly. The fuel cell stack may be associated with an air transport system for conveying an air flow thereto and / or a temperature adjustment assembly for maintaining the fuel cell stack in an appropriate temperature range for generating electricity.

  The present disclosure discloses assemblies, systems, apparatus and methods configured to produce hydrogen gas from one or more feedstocks for use in electrochemical fuel cells or other applications, and the like Relates to an energy generating assembly incorporating In some embodiments, a hydrogen generation assembly and / or an energy generation assembly incorporating the same is suitable for portable device applications. In some embodiments, the hydrogen generation assembly and / or the energy generation assembly incorporating the same does not require a pump and other electrically driven fluid transport system. In some embodiments, the hydrogen generation assembly and / or the energy generation assembly incorporating the same may be a pump or other feed transport configured to draw one or more feed streams from the feed. In some embodiments, including the system, it is a non-pressurized or low pressure supply. In some embodiments, the hydrogen generation assembly and / or the energy generation assembly incorporating the same does not require an electric drive controller. In some embodiments, the hydrogen generation assembly and / or the energy generation assembly incorporating the same includes a controller, in some embodiments, this is an electric drive controller, and some In an embodiment, a controller that is computer controlled or executed by a computer. In some embodiments, the hydrogen generation assembly and the energy generation assembly incorporating the same are designed to produce pure hydrogen gas without the need for a power feed transport system or heating or other temperature regulation assembly. Composed. In some embodiments, the hydrogen generation assembly and / or the energy generation assembly incorporating the same includes an electrically powered feed transport system and / or a heating or other temperature regulation assembly. In some embodiments, a hydrogen generation assembly and / or an energy generation assembly incorporating the same may be activated from an off-operation configuration and transitioned from the activated operation configuration to a hydrogen generation and / or energy generation configuration. Configured to maintain a selected operating structure with minimal user input and / or balance of plant requirements. In some embodiments, the hydrogen generation assembly and / or the energy generation assembly incorporating the same is configured to start using a liquid fuel burner assembly. In some embodiments, the hydrogen generation assembly and / or the energy generation assembly incorporating the same is configured to be activated using a gas fuel burner assembly. In some embodiments, the hydrogen generation assembly and the energy generation assembly incorporating the same may include a recycle stream and a flow rate to regulate the flow rate at which the feed stream is transported to the hydrogen generation region of the fuel processor. A feed transport system configured to utilize at least one of a throttle valve and / or a pressure regulating valve for regulating pressure is included. In some embodiments, the hydrogen generation assembly and / or the energy generation assembly incorporating the same comprises a portable assembly. In some embodiments, the hydrogen generation assembly is configured to generate less than 15 slm hydrogen gas when operating at full capacity, and in some embodiments, less than 10 slm, or less than 5 slm It is comprised so that hydrogen gas may be produced | generated. In some embodiments, an energy generation assembly incorporating a hydrogen generation assembly according to the present disclosure is configured to have a rated power of at least 100 watts and / or 1000 watts or less, and optionally 100- Configured to have a rated power of 400 watts, 200-600 watts and / or 400-800 watts.

  A hydrogen generation assembly according to the present disclosure is illustrated schematically in FIG. The hydrogen generation assembly includes a feed transport system 22 and a fuel processing assembly 31. The fuel processing assembly or system 31 is configured to provide a product hydrogen stream 14 from one or more feed streams 16 that includes hydrogen gas and preferably includes at least substantially pure hydrogen gas. A processor 12 is provided. The feed stream 16 may include at least one carbon-containing feedstock 18. The fuel processor 12 includes any suitable device or combination of such devices that are highly suitable for producing hydrogen gas from the feed stream 16. Accordingly, the fuel processor 12 includes a hydrogen generation region 19 in which an output stream 20 containing hydrogen gas is generated by utilizing any suitable hydrogen generation mechanism or mechanisms. The output stream 20 includes hydrogen gas as at least a main component. The output stream 20 may include one or more additional gaseous components, which may be referred to as a mixed gas stream that includes hydrogen gas as its major component but includes other gases. Region 19 may utilize a suitable catalyst containing layer (bed) or region.

  Examples of suitable mechanisms for generating hydrogen gas from one or more feed streams 16 transported by the feed transport system 22 include steam reforming and autothermal reforming. There, the reforming catalyst is used to produce hydrogen gas from a feed stream 16 comprising a carbon-containing feed 18 and water 17. In the steam reforming process, as shown by a broken line in FIG. 1, the hydrogen generation region 19 includes an appropriate steam reforming catalyst 23. In such an embodiment, the fuel processor may be referred to as a steam reformer, the hydrogen generation zone 19 may be referred to as the reforming zone, and the output or mixed gas stream 20 may be referred to as reformed gasoline (reformate). ) May be called a flow. Examples of suitable steam reforming catalysts include low temperature shift catalyst copper-zinc formulations and chromium formulations sold by Sud-Chemie under the trade name KMA, although others may be used. Other gases typically present in the reformed gasoline stream include carbon monoxide, carbon dioxide, methane, steam and / or unreacted carbon-containing feedstock. In an autothermal reforming reaction, a suitable autothermal reforming catalyst is used to create hydrogen gas from water and a carbon-containing feedstock in the presence of air. When using autothermal reforming, the fuel processor further includes an air transport assembly 55 that is configured to transport an air stream to the hydrogen generation region, as indicated by the dashed lines in FIG. The self-heating hydrogen generation reaction utilizes a main endothermic reaction used in conjunction with an exothermic partial oxidation reaction that generates heat in the hydrogen generation region in response to the start of the initial hydrogen generation reaction.

  Other suitable mechanisms for generating hydrogen gas include pyrolysis of carbon-containing feedstocks and catalytic partial oxidation. In that case, the feed stream does not contain water. Examples of suitable carbon-containing feedstock 18 include at least one hydrocarbon or alcohol. Examples of suitable hydrocarbons include methane, propane, natural gas, diesel, kerosene, gasoline and the like. Examples of suitable alcohols include that the hydrogen generation assembly 10 including methanol, ethanol and polyhydric alcohols (eg, ethylene glycol and propylene glycol) can utilize one or more hydrogen generation mechanisms in the hydrogen generation region 19. Is within the scope of disclosure

  The fuel processing assembly 31 according to the present disclosure may further include a purification or separation region 24 in which the hydrogen rich stream 26 is generated from the output or mixed gas stream, although not required. The hydrogen rich stream 26 includes at least one of a higher hydrogen concentration than the output stream 20 and one or more reduced concentrations of other gases or impurities present in the output stream. The purification region 24 is illustrated schematically in FIG. 1 where the output stream 20 is shown transported to any purification region 24. As shown in FIG. 1, the product hydrogen stream 14 includes at least a portion of the hydrogen rich stream 26. Thus, the hydrogen rich stream 26 may be the same stream and may have the same composition and flow rate. However, some purified hydrogen gas in the hydrogen rich stream 26 can be stored for later use (eg, in a suitable hydrogen storage assembly) and / or consumed by the fuel processing assembly. It is also within the scope of the present disclosure.

  The purification region 24 is not essential, but produces at least one byproduct stream 28. The by-product stream 28 may not contain hydrogen gas or may contain some hydrogen gas. If present, byproduct stream 28 may be discharged, transported to a burner assembly or other combustion source, used as a heated fluid stream, and stored for later use. Or may be utilized and stored or disposed of. By-product stream 28 is produced as a continuous stream in response to transport of output stream 20 to the purification zone, or intermittently, such as in a batch process, or when a by-product portion of the output stream is held at least temporarily in the purification zone. It is within the scope of the disclosure that it can be released from the purification region 24.

  Although not required, the one or more configured to produce one or more by-product streams containing a sufficient amount of hydrogen gas suitable for use as a fuel or feed stream to a heating assembly for a fuel processing system It is within the scope of the present disclosure that the fuel treatment system 31 can include the purification region. In some embodiments, the byproduct stream has a sufficient fuel value that can maintain a hydrogen production region at a desired operating temperature or within a selected temperature range when a heating assembly is present. (Ie, hydrogen content). Thus, although not required, hydrogen gas (eg, 10-30 parts by weight hydrogen gas, 15-25 parts by weight hydrogen gas, 20-30 parts by weight hydrogen gas, at least 10 or 15 parts by weight hydrogen gas, at least 20 parts by weight It is within the scope of the present disclosure that the by-product stream may contain parts by weight of hydrogen gas and the like.

  It is within the scope of the present disclosure that the purification or separation zone and the hydrogen production zone can be housed together in a common shell or housing 68. The separation region is located separately from the hydrogen generation region but is in fluid communication to receive the mixed gas stream from the hydrogen generation region. Is within the scope of the present disclosure.

  The purification region 24 includes any suitable mechanism, device, or combination of these devices configured to reduce the concentration of at least one component of the output stream 20. In most applications, the hydrogen rich stream 26 has a higher hydrogen concentration than the power or mixed gas stream 20. However, a hydrogen-rich stream can have a reduced concentration of one or more non-hydrogen components present in the output stream 20, but can also have an overall hydrogen concentration reduced to a similar or output stream, It is also within the scope of the disclosure. For example, in some applications where the product hydrogen stream 14 may be used, certain impurities or non-hydrogen components are more harmful than others. As a specific example, in conventional fuel cell systems, carbon monoxide can damage the fuel cell stack, even when present at as low as a few ppm. On the other hand, other non-hydrogen components such as water that may be present in the output stream 20 will not damage the stack, even when present at higher concentrations. Thus, in this type of application, a suitable purification zone may not increase the overall hydrogen concentration, but non-hydrogen that is harmful or potentially harmful to the desired application for the product hydrogen stream. The concentration of the component is reduced.

  Examples of suitable equipment for the purification region 24 include one or more hydrogen selective membranes 30, a chemical carbon monoxide removal assembly 32, and a pressure swing adsorption system 38. The purification region 24 may include multiple types of purification devices, and these devices may have the same or different structures and / or may be operated by the same or different mechanisms, Within the scope of the disclosure. As described herein, the hydrogen generating fuel processing assembly 31 includes at least one downstream of at least one purification zone associated with, for example, one or more of the product hydrogen stream, the hydrogen rich stream, and / or the byproduct stream. A restriction orifice or other flow restrictor may be included.

The hydrogen-selective membrane 30 is permeable to hydrogen gas, but at least substantially not otherwise permeable to other components of the output stream 20. The membrane 30 may be formed of any hydrogen permeable material that is appropriate for the operating environment and parameters in which the purification zone 24 is operated. Examples of suitable materials for the membrane 30 include palladium and palladium alloys and particularly thin films of such metals and metal alloys. It has been found that palladium alloys having 35 parts by weight of palladium to 45 parts by weight of copper are particularly effective. A palladium copper alloy containing approximately 40 parts by weight of copper has been found to be particularly effective. However, other relative concentrations and components may be used within the scope of the disclosure. Prepare various membranes, membrane configurations and the same as disclosed in US Pat. Nos. 6,221,117, 6,319,306, and 6,537,352 All of the methods to do are cited herein for reference purposes.

  The chemical carbon monoxide removal assembly 32, when present in the output stream 20, chemically reacts the carbon monoxide and / or other undesirable components of the output stream 20 to other components that are not potentially harmful. It is a device to convert to. An example of a chemical carbon monoxide removal assembly is a water gas shift reactor that produces hydrogen gas and carbon dioxide from water and carbon monoxide, a partial oxidation reactor that is configured to convert carbon monoxide to carbon dioxide, one A methanogenic catalyst zone or bed that converts carbon oxides and hydrogen to methane and water. It is within the scope of the disclosure that the fuel processing assembly 31 can include multiple types and / or multiple chemical removal assemblies 32.

  Pressure swing adsorption (PSA) is based on the principle that a particular gas is more strongly adsorbed onto an adsorbent material than other gases under appropriate temperature and pressure conditions. It is a chemical method that is removed from. In general, it is the impurities that are adsorbed and removed from the output stream 20. The adsorption of the impurity gas occurs at a high pressure. When the pressure is decreasing, the impurities are desorbed from the adsorbent material, thus regenerating the adsorbent material. In general, PSA is a cyclic process and requires at least two beds (beds) for continuous operation (as opposed to batch). Examples of suitable adsorbent materials that can be used in the adsorbent bed are activated carbon and zeolites (especially 5 Angstrom zeolites). The PSA system 38 also provides an example of equipment for use in the purification zone 24 where by-products or removed components are not released directly from the purification zone 23 as a gas stream in parallel with the purification of the output stream. Instead, these by-product components are removed as the adsorbent material regenerates or otherwise is removed from the purification zone.

  In FIG. 1, the purification region 24 is shown in the fuel processor 12. It is within the scope of the disclosure that when region 24 is present, it can be separately located downstream from fuel processor 12, as schematically shown in the dashed line in FIG. It is also within the scope of the disclosure that the purification region 24 can include portions inside and outside the fuel processor 12.

  In FIG. 1, the fuel processor 12 is shown including a shell 68 that includes at least a hydrogen production region and an optional purification region. Shell 68, which may be referred to as a housing, allows steam reformer or other fuel processing mechanism components to move as a unit. This protects the components of the fuel processor 12 from damage by providing a protective housing and also reduces the heating requirements of the fuel processing assembly as the fuel processor components are heated in units. Shell 68 includes, but is not essential, an insulating material 70 such as, for example, a solid insulating material, a blanket insulating material, and / or an air filled cavity. However, it is within the scope of the disclosure that the fuel processor can be formed without a housing or shell. When the fuel processor 12 includes an insulating material 70, the insulating material may be internal to the shell, external, or both. If the insulating material is external to the shell including the reforming and / or purification region described above, the fuel processor 12 may include an outer cover or outer jacket 72 outside the insulating material, as schematically shown in FIG. . The fuel processing assembly may be implemented in a different shell with a shell that includes additional components of the fuel processing assembly that includes the feed transport system 22 (or portions thereof) and / or additional fuel cell systems. It is within the scope of the present disclosure for such components to be included. It is also within the scope of the present disclosure that the fuel processing assembly 31 may not include the shell 68.

  It is further within the scope of the disclosure that one or more components of the fuel processing assembly 31 may extend beyond the shell or may be located at least outside the shell 68. For example, as described, the purification region 24 may be located outside the shell 68, such as a purification region that is directly coupled to the shell (as illustrated schematically in FIG. 5), or The fluid is in communication by a suitable fluid transfer conduit (as indicated by the dashed line in FIG. 1) but may be spaced from the shell. As another example, a portion of the hydrogen production region 19 (eg, a portion of one or more reforming catalyst beds) is schematically illustrated by the alternate long and short dashed line representing another alternative shell structure in FIG. As such, it may extend beyond the shell.

  In the exemplary non-exclusive embodiment in FIG. 1, the fuel processing system 31 includes a temperature regulation assembly in the form of a hydrogen generation region 19 and a heating assembly 60. The heating assembly 60 is typically configured to produce a heated discharge stream or combustion stream 66 from the heated fuel stream 64 when combusting in the presence of air. This discharge or combustion stream 66 is schematically illustrated in FIG. The heating assembly 60 may utilize any suitable structure for generating a heated discharge stream 66, such as a burner or a combustion catalyst in which fuel is combusted with air to generate a heated discharge stream. The heating assembly 60 may include an igniter or ignition source 89 that is configured to initiate combustion of fuel and thereby generate a discharge stream 66. Examples of suitable ignition sources include one or more of spark plugs, glow plugs, combustion catalysts, pilot lights, piezoelectric igniters, and the like.

  In some fuel processing assemblies according to the present disclosure, the heating assembly 60 includes a burner assembly 62, which may be referred to as a combustion base or combustion driven heating assembly. In the combustion-based heating assembly, the heating assembly 60 receives at least one fuel stream 64 and in the presence of air to provide a hot combustion stream 66 that can be used to heat at least the hydrogen production region 19 of the fuel processor. The fuel stream is configured to burn. As described in more detail herein, air can be transported to the heating assembly via various mechanisms. In FIG. 1, an air flow 74 is shown, but in addition to or in place of the air flow transported to the heating assembly, at least one of the fuel streams 64 is transported to the heating assembly, and / or Or, it is within the scope of the disclosure to be drawn from the environment in which the heating assembly is utilized.

  It is within the scope of the disclosure that the combustion stream 66 can be used additionally or alternatively to heat other portions of the fuel processing assembly and / or the fuel cell system in which the heating assembly 60 is used. It is within the scope of the present disclosure that other configurations and types of heating assembly 60 may be utilized. As an example, the heating assembly 60 is an electrically driven heating assembly that is configured to heat at least a hydrogen generation region of the fuel processing assembly by generating heat using at least one heating element, eg, a resistive heating element. There may be. Thus, it is not necessary for the heating assembly 60 to receive and burn the combustible fuel stream to heat the hydrogen production zone 19 to the appropriate hydrogen production temperature. An additional non-exclusive example of a heating assembly that can utilize the hydrogen generation assembly, hydrogen generation fuel processing assembly, fuel cell system, etc. disclosed herein is filed on Sep. 13, 2005 under the name “Hydrogen”. -Producing Fuel Processing Assemblies, Heating Assemblies, and Methods of Operating the Same ", U.S. Patent Application Publication No. 11 / 226,810, which is incorporated herein by reference in its entirety.

  It is within the scope of the present disclosure that the heating assembly 60 is housed in a common shell or housing 68 with a hydrogen generation region and / or a separation region, as schematically illustrated in FIG. However, this structure is not essential. Although the heating assembly may be separately located with respect to the hydrogen generation region, it is within the scope of the present disclosure that it is in thermal communication and / or fluid communication to provide at least the desired heating of the hydrogen generation region. The heating assembly may be located partially or completely within the fuel processor 12 (such as at least part within the shell 68) and / or at least part or all of the heating assembly may be located external to the fuel processor. As shown graphically to be within the scope of the present disclosure, in FIG. 1 the heating assembly 60 is shown in an overlapping relationship with the fuel processor 12. In this latter (externally located) embodiment, hot combustion gases from the burner assembly are transported via appropriate heat transfer conduits to the fuel processor or other parts of the heated system.

Depending on the configuration of the hydrogen generation assembly 10 and the fuel processing system 31, the heating assembly 60 may be a feed transport system, feed stream, hydrogen generation zone, purification (or separation) zone, or any combination of these elements, or These selected elements can be configured to heat. Heating the feed stream can include evaporating a liquid reactant stream or component of the hydrogen generation fluid used to generate hydrogen gas in the hydrogen generation zone. In such an embodiment, the fuel processing system may be described as including an evaporation region 69. The heating assembly 60 may also be configured to heat other members of the hydrogen generation assembly 10. For example, the heated discharge stream may also be configured to heat a pressure vessel or other vessel containing heated fuel and / or hydrogen generating fluid that forms at least a portion of the feed stream 16 and the fuel stream 64. Although not required, increasing the temperature of the container can increase the pressure of the fluid stored in the container, which is desirable in some applications.

  As an example of the temperature that can be obtained and / or maintained in the hydrogen production zone 19 by using the heating assembly 60, the steam reformer operates at a temperature generally in the range of 200 ° C to 900 ° C. Temperatures outside this range are also within the disclosure. When the carbon-containing feedstock is methanol, the steam reforming reaction generally operates at a temperature in the range of approximately 200-500 ° C. Exemplary subsets of this range include 350-450 ° C, 375-425 ° C, and 375-400 ° C. When the carbon-containing feedstock is a hydrocarbon, ethanol or other alcohol, a temperature range of approximately 400-900 ° C is generally used for the steam reforming reaction. Exemplary subsets of this range include 750-850 ° C, 725-825 ° C, 650-750 ° C, 700-800 ° C, 700-900 ° C, 500-800 ° C, 400-600 ° C, and 600-800 ° C. Including. It is within the scope of the present disclosure to include two or more regions or portions for the hydrogen generation region, each of which can be operated at the same or different temperatures. For example, when the hydrogen generating fluid includes hydrocarbons, in some embodiments, it includes two different hydrogen generating portions or regions, one of which over the other to provide a pre-reforming region. It may be desirable to operate at lower temperatures. In such embodiments, the fuel processing system may alternatively be described as including two or more hydrogen production regions.

  A hydrogen generation fuel processing assembly or hydrogen generation assembly 10 in the present disclosure is configured to selectively transport at least one feed stream 16 to at least a hydrogen generation region of the fuel processing / generation assembly. 22 may be included. In some embodiments, the feed transport system is configured to heat at least the hydrogen production region 19 to heat (and selectively maintain) at least the hydrogen production region 19 at a suitable hydrogen production temperature. Configured to at least selectively transport the fuel stream 64 to a burner 62 or other heating assembly 60. The feed transport system 22 may utilize any suitable transport mechanism (eg, positive movement or other suitable pump or mechanism that drives liquid flow). In some embodiments of the feed transport system 22 according to the present disclosure, the transport system does not require the use of a pump or other electrically driven fluid transport mechanism, and at least the feed stream and / or the fuel stream. It is configured to transport one.

  The feed transport system 22 is transported to the hydrogen generation region 19 of the fuel processing system, including the two feed streams 11, ie, at least one hydrogen generation fluid 15, in the embodiment shown schematically in FIG. A heated fuel feedstock configured to transport a hydrogen production fluid feedstream or feedstream 16 configured to be transported to a heating assembly 60 that includes at least one combustible fuel 13. It is configured to transport stream 64.

  Although a single feed stream 16 is shown in FIG. 1, it is possible that multiple feed streams 16 can be used and that these feed streams can contain the same or different feeds. Within the scope of the disclosure. This is schematically illustrated by including a second feed stream 16 in the dashed line of FIG. Similarly, FIG. 1 also shows (although not required) that each feed stream 16 may be associated with a different feed transport system 22 or portion thereof, in a dashed line. For example, when multiple feed transport systems 22 are utilized, the system may draw (but is not essential) at least a portion of the exit stream from a common source. When the feed stream 16 includes more than one component (eg, carbon-containing feed and water), these components can be transported in the same or different feed streams.

  As schematically illustrated in the exemplary embodiment shown in FIG. 1, when the heating assembly forms part of the fuel processing assembly, the fuel processing assembly includes at least two feed streams 11, That is, it can be described as being configured to receive the fluid feed stream 16 and the fuel feed stream 64. It is within the scope of the present disclosure that these fluid feed stream 16 and fuel feed stream 64 can be transported from the same or different transport systems, as shown in dashed line FIG. The fluid feed stream 16 and the fuel feed stream 64 may have different compositions, at least one common component, may not have a common component, or may have the same composition. This is also within the scope of the present disclosure. The feed transport system may include or be in fluid communication with any type and / or number of sources or sources 112 suitable for the feed stream and fuel stream components being transported.

  The hydrogen production fluid 15 can include one or more fluids that can be utilized as reactants to produce the product hydrogen stream 14 as described above. The configuration of the hydrogen generation fluid 15 may be selected based on the configuration of the hydrogen generation assembly 10 and / or the mechanism by which hydrogen is generated in the hydrogen generation region. For example, the hydrogen generating fluid 15 includes at least one carbon-containing feedstock, water or a combination of water and a carbon-containing feedstock. An example of a carbon-containing feedstock is that described above in this specification. If the hydrogen production zone is configured to accept water and carbon-containing feedstock as reactants that produce hydrogen gas, one or both of these reactants can be supplied as a hydrogen production fluid by the feed transport system.

  For example, when a carbon-containing feedstock is used that can be mixed with water, such as methanol or other water-soluble alcohols, the feed transport system transports a hydrogen generating fluid 15 that includes a mixture of water and carbon-containing feedstock. (But is not required). The ratio of water to carbon-containing feedstock in this type of fluid stream can vary according to the particular carbon-containing feedstock used, user preferences, hydrogen production zone design, and other factors. The molecular ratio of water to carbon can typically be approximately 1: 1 to 3: 1. Mixtures of water and methanol can be transported in molecular ratios generally around 1: 1 (31 vol% (volume%) water, 69 vol% methanol), while mixtures of hydrocarbons or other alcohols are water to carbon. Can be transported at molecular ratios typically greater than 1: 1.

  As a further example, the reformed feed stream 16 can include approximately 25-75 vol% methanol or ethanol or other suitable water-soluble carbon-containing feedstock and approximately 25-75 vol% water. For a feed stream formed (at least substantially) with methanol and water, this feed stream generally comprises approximately 50-75 vol% methanol and approximately 25-50 vol% water. A feed stream comprising ethanol or other water soluble alcohols generally comprises approximately 25-60 vol% alcohol and approximately 40-75 vol% water. An example of a particularly suitable feed stream for a hydrogen-generating assembly that utilizes steam reforming or autothermal reforming reactions includes 69 vol% methanol and 31 vol% water. However, other compositions and liquid carbon-containing feedstocks may be used within the scope of this disclosure.

  Although not required, this type of feed stream, which includes both water and at least one carbon-containing feedstock, heats the feed stream for the hydrogen production zone 19 and at least the hydrogen production zone of the fuel processing assembly. It is within the scope of the present disclosure that it can be used as a combustible fuel stream for a heating assembly configured as such. When water and water-soluble liquid carbon-containing feeds are mixed before use, a potential advantage of this type of structure is that a hydrogen generation assembly that generates hydrogen gas from water and carbon-containing feeds is a single feed. It is not necessary to include more than 112. Otherwise, the hydrogen generation assembly only requires a feedstock containing water and carbon.

  It is within the scope of the present disclosure that the feed transport system 22 can transport components of the hydrogen production stream or feed stream to two or more streams of fuel processing assemblies having the same or different compositions. For example, when the fuel processor is configured to generate hydrogen gas from a carbon-containing feedstock and water, these components are typically delivered in separate streams, and optionally if not mixed with each other , As indicated in FIG. 1 by reference numbers 17 and 18 indicating optionally different feed streams (at least both streams evaporate or otherwise become gaseous).

  It is within the scope of the present disclosure that the heated fuel 13 can include any flammable liquid and / or gas suitable for being consumed by the heating assembly 60 to provide the desired heat output. Some heated fuels 13 according to the present disclosure are gases when transported and burned by the heating assembly 60, while others are transported to the heating assembly as a liquid stream. An example of a suitable heated fuel includes the carbon-containing feedstocks described above (eg, methanol, methane, ethane, ethanol, ethylene, propane, propylene, butane and butanes). Further examples include low molecular weight cohesive fuels such as liquefied petroleum gas, ammonia, light weight amines, dimethyl ether and low molecular weight hydrocarbons. Although not required in all embodiments, the heated fuel stream and the hydrogen generating fluid stream can have different individual or total compositions and can be released from the feed transport system in different phases. For example, when one of the streams is a liquid stream, the other may be a gas stream. In some embodiments, both streams may be liquid streams. In some embodiments, both streams may be gas streams. A hydrogen generation assembly that includes a temperature adjustment assembly in the form of a cooling assembly instead of a heating assembly (such as used when an exothermic hydrogen generation process is utilized instead of an endothermic method such as steam reforming) In this embodiment, it is within the scope of the present disclosure that the feed transport system can be configured to supply a fuel or coolant stream to the assembly. Any suitable fuel or cooling fluid can be used.

  Exemplary non-exclusive embodiments of suitable feed transport systems that can be used in the hydrogen generating fuel processing assembly (or hydrogen generating assembly) in the present disclosure are described in US patent application Ser. No. 11 / 228,637, 11 / 096,827 and 60 / 623,894, the entire disclosures of which are incorporated herein for all reference purposes. The above incorporated applications are also fuel processing assemblies, fuel cell systems, components therefor, and other components that can be selectively used and / or disclosed, illustrated and / or incorporated herein. Additional examples of methods of operating the same that can be integrated with are disclosed. Additional illustrated examples of suitable hydrogen generation assemblies and parts thereof include U.S. Pat. Nos. 6,221,117, 5,997,594, 5,861,137, and U.S. Patent Application Publication Nos. 2001/0045061, 2003/0192251, and 2003/0223926, which are ongoing. The complete disclosures of the above-mentioned patents and patent applications can all be incorporated herein for reference purposes. Additional examples are disclosed in US patent application Ser. Nos. 10 / 945,783, 11 / 226,810 and 11 / 228,637. The entire disclosures of which are incorporated herein by reference for all purposes.

  As will be described, the product hydrogen stream 14 may be used in a variety of applications, including applications where high purity hydrogen gas is utilized. An example of this type of application is as a fuel or feed stream for a fuel cell stack. The fuel cell stack is a device that generates a potential from a proton supply source such as hydrogen gas and an oxidant supply source such as oxygen gas. Accordingly, the hydrogen generation assembly 10 includes or is coupled to at least a portion of the fuel cell stack 40 that is configured to receive the generated hydrogen stream 14 and at least a portion of the air or other oxidant stream 81 to generate power. Can be done. This is schematically illustrated in FIG. 2 where the fuel cell stack is shown at 40 and produces a current, which is schematically illustrated at 41. The air flow 81 can be transported to the fuel cell stack via any suitable mechanism including passive or active mechanisms and motorized or manual mechanisms. When coupled to the fuel cell stack 40, the hydrogen generation assembly may be referred to as an energy generation system or fuel cell system 42.

  As used herein, the hydrogen generation assembly 10 may be referred to as a fuel processing system, a fuel processing assembly, and / or a hydrogen generating fuel processing system (or assembly). As used herein, the energy generation system 42 may be referred to as a fuel cell system or a hydrogen generation fuel cell system. This application incorporates by reference a number of different applications that disclose fuel processing assemblies, fuel cell systems, or parts thereof. It is understood that these systems and components, including variations disclosed, illustrated and incorporated herein, can be selectively combined and used or integrated without departing from the scope of the present disclosure. Within the scope of the disclosure.

  The stack 40 includes at least one fuel cell 44 and typically a plurality of oxidants such as air, oxygen rich air, oxygen gas, and at least one fuel cell configured to generate current from a portion of the product hydrogen stream 14 being transported. The fuel cell 44 is included. The fuel cell stack generally includes a plurality of fuel cells coupled between a common end plate 48 that includes fluid transport / removal conduits. However, this structure is not necessary for all embodiments. Examples of suitable fuel cells include proton exchange membrane (PEM) fuel cells and alkaline fuel cells. Others include solid oxide fuel cells, phosphoric acid fuel cells and molten carbonate fuel cells.

The fuel cell stack 40 can have any suitable structure. Examples of fuel cell stacks and parts thereof are described in US Pat. Nos. 4,214,969, 4,583,583, 5,300,370, 5,484,666, 5 , 879,826, 6,057,053, and 6,403,249, which are hereby incorporated by reference in their entirety. Additional examples are disclosed in US Provisional Application Nos. 60 / 623,156 and 60 / 630,710. The entirety of which is incorporated herein by reference. Additional exemplary, non-exclusive examples in suitable fuel cell systems, stacks and components thereof that can be used in fuel cell systems, including hydrogen generating fuel cell systems including hydrogen generating fuel processing assemblies according to the present disclosure. Is disclosed in U.S. Patent Application No. _, filed October 28, 2005, entitled "Fuel Cell Stack Compression Systems, and Fuel Cell Stacks and Fuel Cell Systems Incorporating the Same". The entirety of which is incorporated herein by reference.
Additional examples of fuel cell systems, stacks and components thereof that can be used in a fuel cell system, including a hydrogen generating fuel cell system including a hydrogen generating fuel processing assembly according to the present disclosure, were filed on June 10, 2005. It is disclosed in US patent application Ser. No. 11 / 150,615, entitled “Partitioned Fuel Cell Stacks and Fuel Cell Systems Including the Same”. The entirety of which is incorporated herein by reference.

  In other applications where it is desired to have a source of hydrogen gas, the hydrogen generation assembly 10 according to the present disclosure is used and / or the present disclosure for generating hydrogen gas for storage and later consumption. It is within the scope of the present disclosure that a hydrogen generation assembly 10 according to can be used. In other words, while the hydrogen generation assembly 10 according to the present disclosure can be utilized in a fuel cell stack to provide a fuel cell system that satisfies an applied electrical load, the hydrogen generation assembly is independent of the fuel cell stack. It is also within the scope of the present disclosure.

  The energy generation or fuel cell system 42 is configured to supply power that matches the load applied from the at least one energy consuming device 46. Examples of consumer equipment include, but are not limited to, automobiles, recreational vehicles (RVs), construction vehicles or industrial vehicles, boats and other sea aircraft, and one or more residences, commercial offices or buildings, suburbs, tools, Lighting and lighting assemblies, radios, equipment (including household equipment), computers, industrial equipment, signal and communication equipment, radios, boats, recreational vehicles or other electric drive parts on vehicles, battery chargers, automatic battery chargers, mobile Also includes any combination of equipment, mobile tools, emergency response units, life support devices, patient monitoring devices, and the balance of plant electrical requirements of the energy generation system 42 of which the fuel cell stack 40 forms part. As used herein, the energy consuming device 46 schematically and generally represents one or more energy consuming devices configured to draw power from an energy generation system or fuel cell system according to the present disclosure. Used as shown. An energy generation system according to the present disclosure that includes such a system, including a hydrogen generation assembly (or hydrogen generation fuel processing assembly) in the present disclosure, as shown generally at 56 in FIG. It is within the scope of the present disclosure that it can be integrated with or otherwise coupled to, or housed together with, at least one energy consuming device to provide an assembly or system.

  With respect to the portable energy generation system according to the present disclosure, the ratio at which the hydrogen generation assembly is configured to generate hydrogen gas and the rated power of the fuel cell stack 40 may be configured to be output by the system 22. Contribute or otherwise define the number and / or type of Thus, although not required for all fuel energy generation systems (or hydrogen generation fuel cell systems), including (but not necessarily) a smaller portable energy generation system according to the present disclosure, It can be designed or otherwise configured to have a rated / scheduled maximum output of 1000 watts or less and a corresponding hydrogen gas production rate. In some embodiments, the system can be designed or otherwise configured to have a rated / planned maximum power output of 500 watts or less and a corresponding hydrogen gas production rate. In some embodiments, the system may be designed to have a rated / scheduled maximum power and a corresponding hydrogen gas production rate of 300 watts or less, or even 250 watts, or otherwise. If not, it can be configured. This system generally has a rating or maximum output of at least 100 watts. However, this is not necessary for all embodiments. Illustrative, non-exclusive examples of power of 1000 watts or less that can be used by the systems in this disclosure are, but are not limited to, 800-500 watts, 500-750 watts, 750-1000 watts 200-500 Watts, 250-500 Watts, 300-600 Watts, and 400-800 Watts. Illustrative non-exclusive examples of 500 watts or less of output that may be used by the systems in this disclosure are, but are not limited to, 25-500 watts, 50-200 watts, 50-250 watts 150-250 Watts, 350-400 Watts, 100-400 Watts, 100-300 Watts, and 250-450 Watts. Illustrative non-exclusive examples of 300 watts or less of output that may be used by the systems in this disclosure are, but are not limited to, 100-300 watts, 75-300 watts, 100-200 watts 200-300 Watts, 150-300 Watts, and 250-300 Watts. In general, these systems are relatively lightweight and compact so that they are sized for manual transfer by an individual.

  When the fuel cell system 42 is configured to have a rated power of less than 1 kW as described above, the corresponding hydrogen generation assembly 10 will properly supply the hydrogen gas in the generated hydrogen stream 14 to produce this power output. It may be configured to be provided to one or more fuel cell stacks at a flow rate. For example, the hydrogen generation assembly illustrated herein may be configured to generate less than 20 slm of hydrogen gas when operating at full capacity. The illustrated subset of this range includes less than 15 slm, less than 10 slm, less than 5 slm, 13-15 slm, 3-5 slm and 2-4 slm hydrogen gas. For a system 44 rated to deliver 250 watts / hour, a suitable capacity for the exemplary non-limiting example hydrogen generation assembly 10 is 3-4 slm hydrogen gas.

  However, a hydrogen generation assembly according to the present disclosure (and an energy generation system incorporating the same) depends on the desired flow rate of hydrogen gas in the product hydrogen stream 14, the desired rated output of the energy generation system, and the energy generation assembly. It can be constructed on any suitable scale, depending on the type and / or number of energy consuming equipment to be output, the size limitations available for the hydrogen generation assembly and / or energy generation assembly, etc. Within range. In some embodiments, rated (desired) in the range of 1-2 kW having an assembly that includes a hydrogen generation assembly configured to provide hydrogen gas to provide the necessary power to satisfy an applied load or the like. It may be preferred to provide an energy generating assembly according to the present disclosure having an output. In other applications, it is preferable to have an output in the range of 4-6 kW for the assembly, such as a home or other residential area, small office, or other energy consuming equipment with similar energy demands. sell.

  Embodiments of a hydrogen generation assembly, a fuel processing assembly, a feed transport system, a fuel cell stack, and / or a fuel cell system as disclosed, illustrated and / or incorporated herein are It is within the scope of the present disclosure that it can be utilized in a combination of two or more of the corresponding parts to increase. For example, if a particular embodiment of the hydrogen generation assembly is configured to produce 3-4 slm hydrogen gas, two such assemblies may be used to produce 6-8 slm hydrogen gas. it can. Accordingly, the assemblies and systems disclosed herein may be referred to as measurable systems. The hydrogen generation assembly, fuel processing assembly, fuel cell stack, fuel processor and / or heating assembly described, illustrated and / or incorporated herein may be configured as a modular unit that can be selectively interconnected together. That is within the scope of the present disclosure.

  The fuel cell stack 40 can accept the entire product hydrogen stream 14. Some or all of the stream 14 may additionally or alternatively be transported to other hydrogen consuming processes via suitable conduits and may be burned for fuel or heat. Well, or it can be stored for later use. As an example, the hydrogen storage device 50 is shown by a one-dot chain line in FIG. The instrument 50 is configured to store at least a portion of the product hydrogen stream 14. For example, excess hydrogen gas can be stored in the device 50 when the demand for hydrogen gas by the stack 40 is less than the hydrogen output of the fuel processor 12. An example of suitable hydrogen storage includes hydride beds and pressurized tanks. Although not required, the advantage of the fuel processing assembly 31 or fuel cell system 42 that includes a supply of hydrogen is that this supply uses the stack 40 or this stream 14 in situations where the fuel processor 12 is unable to meet the hydrogen demand. It can be used to meet the hydrogen demand of other applications. Examples of these situations include when the fuel processor is started from a cool or inactive state, ramped from idle (heated and / or pressurized), offline for maintenance or under repair One time and when the fuel cell stack or application requires a flow rate of hydrogen gas that is greater than the maximum available production from the fuel processor. Additionally or alternatively, the stored hydrogen can be used as a combustible fuel stream to heat the fuel processing assembly or fuel cell system. Fuel processing assemblies that are not directly related to the fuel cell stack can still include at least one hydrogen storage device, whereby the product hydrogen stream from these fuel processing assemblies is stored for later use. It also makes it possible.

  The fuel cell system 42 may include a battery 52 or other suitable electrical storage device configured to store potential or power generated by the stack 40. Similar to the description above for excess hydrogen, the fuel cell stack 40 produces more output than is necessary to satisfy the load applied or operated by the equipment 46 including the required load on the fuel cell system 42. sell. In further analogy to the above description of excess hydrogen gas, this excess output can be used in other applications outside the fuel cell system and / or stored for later use by the fuel cell system. . For example, a battery or other storage device provides an output for use by the system 42 during startup, or for use by other applications when the system is not producing electricity and / or hydrogen gas. can do. In FIG. 2, the flow conditioning structure is shown generally at 54 for selectively transporting the hydrogen and fuel cell stack outputs to the device 50 and the battery, respectively, to extract the stored hydrogen and power. Fig. 2 schematically represents any suitable manifold, valve, controller, switch, etc.

  It is within the scope of the present disclosure that the hydrogen generation assembly and / or the fuel cell system may not include a computerized controller and control system. In such an embodiment, the system may be simpler and with lower plant requirements in that the equivalent assembly or system including the controller may not include many sensors, communication couplings, actuators, etc. Balance can be taken. However, in some embodiments it may be preferred to include a controller to coordinate the operation of the assembly or system, such as to automate one or more operations of the assembly or system. And in FIG. 3, an example of a controller is schematically illustrated at 88 and shown in communication with the feed transport system 22 and the heating assembly 60 of the hydrogen generation assembly. In this type of configuration, the controller can be configured to control and / or coordinate at least activation of the hydrogen generation assembly. Such a controller may additionally or alternatively control and / or adjust the hydrogen production operating state of the assembly. The controller 88 can be powered by any suitable power source (eg, battery 52). For example, it is within the scope of the present disclosure for the controller 88 to be driven by a power source other than the battery 52, as shown at 52 'in FIG. It is within the scope of the present disclosure that the controller 88 may communicate with the hydrogen generation assembly and / or other components of the fuel cell system, for example to monitor and / or control its operation. This type of controller is schematically illustrated in FIG. 4 and is optional for fuel processing assemblies (eg, hydrogen generation region 19 and purification region 24) and components of fuel cell stack 40 (any one-way or two-way communication). The contact is indicated (via a suitable communication link).

  As indicated by the dashed lines in FIG. 5, the fuel processing assembly 10 according to the present disclosure provides a feed stream 16 such as a liquid feed stream 16 (or a liquid component of a stream of water 17 or a stream of liquid carbon containing feed 18. And a vaporization zone 69 configured to vaporize the feed stream (or portion thereof) prior to transport to the hydrogen generation zone 19 of the fuel processor 12. As shown schematically in FIG. 5, the heated combustion stream 66 from the heating assembly is used to evaporate the feed stream in the evaporation zone 69 and / or otherwise heat the feed stream. Can do. It is within the scope of the disclosure that the fuel processor 12 can be constructed without an evaporation zone and / or that the fuel processor is configured to accept a gas or evaporated feed stream. It is also within the scope of the present disclosure that when the evaporation region 69 is present, this region 69 extends partially or completely outside the shell 68 (if present).

  The fuel processor 12, heating assembly 60 and feed transport system 22 according to the present disclosure may be configured in any arrangement described, illustrated and / or incorporated herein. In some embodiments, features or aspects from one or more of the above-described configurations may be combined with each other and / or with additional features described herein. For example, a fuel processing assembly 10 that includes at least one purification region 24 may house both the hydrogen generation region 19 and at least a portion of the purification region in a housing that is selectively located within the shell 68 of the fuel processor. (But not essential) is within the scope of the present disclosure. This is schematically illustrated in FIG. 6, in which at least a reforming (or other) catalyst 23 used to produce a mixed gas stream from a feed stream that is transported to a hydrogen production zone. Reference numeral 25 generally indicates the hydrogen generation region 19 of the fuel processor, along with the hydrogen generation region contained within the containing housing or vessel 27.

  As indicated by the dashed lines in FIG. 6, the shell 27 (and thus the region 25) may also include the purification region 24, although not essential. For example, as illustrated by the dashed line in FIG. 6, when a purification region is present in the housing, the purification region includes one or more hydrogen-selective membranes 30 and / or chemical carbon monoxide removal assemblies 32. sell. Therefore, the region 25 can be described as a hydrogen generation purification region when it includes the hydrogen generation region 19 and the purification region 24. It is within the scope of the disclosure that any of the regions 19 and 24 described, illustrated and / or incorporated herein can be used in region 25. When region 25 does not include a purification region, it may simply be described as a hydrogen generation region 19 that includes a housing 27. When the housing 27 includes a purification region 24, the fuel processing assembly includes one or more additional purification regions (e.g., may include the same or different purification devices / mechanisms) outside the housing 27 (i.e., from downstream). It is still within the scope of the present disclosure. The fuel processing assembly illustrated herein includes a hydrogen generation region included in a housing that may also optionally include a purification region. As also illustrated in FIG. 6, it is within the scope of the present disclosure that when the evaporation region 69 is present, the evaporation region 69 can extend partially or completely into the housing 27.

  An illustrative and less schematic example of a fuel processor that includes a hydrogen production region on at least the purification region 24 housed in a common sealed shell 27 is shown in FIGS. In an exemplary, non-limiting embodiment, the hydrogen generation zone 19 includes a flow reforming catalyst 23 and the purification zone 24 is supported within the shell to receive the mixed gas stream 20 that results from the reforming reaction. And at least one hydrogen-selective membrane 30 arranged to divide the mixed gas stream 20 into a hydrogen-rich stream that forms the product hydrogen stream 14 and a by-product stream 28. In one example, perhaps best shown in FIG. 8, the hydrogen production zone is separated from the membrane by a catalyst plate 267 having an opening at the end of the hydrogen production zone into which the feed stream is introduced. The reformed gasoline or mixed gas stream produced in the hydrogen production zone flows through these openings that contact the mixed gas or feed at the surface of the membrane 30. The portion of the mixed gas stream that passes through the membrane forms a hydrogen rich stream 26 that can be withdrawn from the shell 27, such as to produce a product hydrogen stream 14. On the other hand, the portion of the mixed gas flow that does not pass through the membrane 30 is withdrawn from the shell as a by-product flow 28.

  As shown, the shell 27 includes end plates 262 and 264 which together define a sealed pressure vessel having an internal compartment 265 in which a hydrogen generation region and a separation region are supported. It is configured to be fixed. Any suitable process may be utilized to seal the portions of shell 27 together. A support 266 for the membrane 30 is also shown. The support 266 should be formed of a porous body through which a portion of the mixed gas flow that permeates the membrane 30 flows. Various support plates 268 and sealing gaskets 270 are also shown.

  It is within the scope of the present disclosure that more than a single membrane 30 or other purification device can be used in a single shell 27 and / or fuel processing assembly 31. This is schematically illustrated in the dashed line in FIG. 8, which shows the methane production catalyst 32 near the output port that draws the hydrogen rich stream from the shell. In such embodiments, the methanation (or other carbon monoxide removal) catalyst may be present at any suitable location downstream of the hydrogen selective membrane. The methanation catalyst can also be located in a fluid conduit that extends in fluid communication from the shell and in which a hydrogen-rich stream flows from the shell.

  Another example of a suitable configuration for a fuel processor that includes a sealed shell 27 that includes a hydrogen generation region 19 and at least one purification (or separation) region 24 is shown in FIGS. Accordingly, FIGS. 9-11 may be shown as providing an additional example of a suitable hydrogen generation region that may be used in a hydrogen generating fuel processing assembly and fuel cell system in accordance with the present disclosure. In the illustrated example, the shell 27 is formed from plate or shell portions 262 and 264 that define an interior compartment 265 that contains a hydrogen generation region and optionally one or more purification regions. The exemplary elongated shape of the shell and corresponding hydrogen generation region 19 is not essential, and other shapes and configurations may be used within the scope of this disclosure. 9 and 10, an optional mount 272 is shown protruding from the shell 27. Mount 272 may be utilized to secure the shell in a desired location in housing 68 at the remainder of the site where the fuel processor and / or fuel processing assembly is located. The number and configuration of these optional mounts can vary within the scope of the present disclosure.

  Similar to the example of FIGS. 7 and 8, the housing is sealed in that the end plate of the housing can be welded or otherwise sealed together after incorporating the internal components contained therein. It may be a stopped housing. However, welding or other sealing of the housing is not necessary for all embodiments. Accordingly, it is within the scope of the present disclosure that a housing or other container configured to be repeatedly disassembled without breaking the housing or otherwise opened and subsequently reassembled can be used. It is. As described and disclosed in the above incorporated US patent application Ser. No. 10 / 945,783, various seals around the hydrogen selective membrane can be welded, brazed, diffusion bonded, or membranes. It is within the scope of the present disclosure that can be formed by other methods that are actually spent to form part of the seal.

  9-11 and perhaps best shown in FIG. 10, the hydrogen generation region 19 is a catalyst region or catalyst such as the reforming catalyst 23 for a hydrogen generation reaction that takes place in the hydrogen generation region. A compartment 274 sized to receive a sufficient amount of Also shown is an access port 276 that extends linearly from the catalyst region in the plane of the catalyst region and parallel to the long axis of the catalyst region. This type of structure, where the access port does not include elbows or other turns, is not required, but can facilitate catalyst loading and unloading (ie removal) more easily. For example, linearly extending the access port allows the catalyst to be injected through the access port into the catalyst area or bed to compress or otherwise transport or place the catalyst in this area. Even the introduction of rods or other members is allowed.

  As shown in FIGS. 10 and 11, and perhaps best shown in FIG. 11, the shell 27 includes a plurality of hydrogen selective membranes 30. These membranes are supported in spaced relation to each other, with various gaskets and spacers used to define the flow paths between the membranes for mixed gas (or reformate gasoline) flow. These streams include those that contain purified hydrogen gas that permeates through one of the membranes, and those that contain a portion of the mixed gas stream that does not permeate the membrane and forms a by-product stream. As shown, the hydrogen production region is housed by three hydrogen selective membranes, a frame, etc. spaced from each other by various gaskets, screens or other porous support layers. It is within the scope of the present disclosure that more or fewer membranes and corresponding supports, plates, gaskets, etc. can be used without departing from the scope of the present application. For example, by including an additional membrane, the reformed hydrogen gas from the mixed gas stream produced in the hydrogen production region can be increased.

  As shown, the plates and gaskets are dimensioned by an asymmetric shape so that these parts can only be present in a predetermined configuration of the housing. This is not essential, but this may assist in the assembly of the part. This is because these members do not accidentally fall back or be placed upside down. In one example of a suitable asymmetric shape, the corner regions 278 of the various parts in the shell are allowed to be inserted into other corners so that only one of the corresponding corner regions in the inner compartment of the shell is allowed to be inserted. It has a shape different from the partial area. Thus, the shell can be described as being adapted or indexed to define the orientation of gaskets, frames, supports and similar parts laminated therein.

  In FIG. 11, several feed plates are shown including (optional) spaced mixing bars 280. The mixing bar facilitates the turbulence of the mixed gas stream transported in contact with the adjacent hydrogen-selective membrane, thereby facilitating the contact between the hydrogen gas and the membrane, thereby allowing the hydrogen gas to permeate through the membrane. Promote. When the mixing bar is present, it is preferable to define gas flow paths on both sides thereof, and it is preferable not to make adjacent membranes contact.

  The shell 27 can further include a chemical purification zone, such as a zone containing a suitable methanation catalyst 32. Additionally or alternatively, when a methanation catalyst is present, the methane purification catalyst is downstream of the shell 27, such as in a conduit where a hydrogen rich stream exits the housing, as shown by the dashed line in FIG. May be included.

  An exemplary, non-limiting embodiment of a hydrogen generation assembly 10 according to the present disclosure is shown schematically in FIG. The hydrogen generation assembly shown in FIG. 12 includes a hydrogen generation region 19 that includes a steam reforming catalyst 23 and a hydrogen generation stream 15 (ie, one or more feed streams 16) that contains water 17 and a carbon-containing feed 18. It can be described as being configured to produce hydrogen gas via a steam reforming reaction that includes. Thus, the illustrated hydrogen generation assembly described in this example includes a flow reformer with a hydrogen generation zone called a reforming zone and a mixed gas stream 20 produced in the hydrogen generation zone called a raffinate stream. May be called.

  In order to provide specific examples that are not exclusive or essential, in the following description, the carbon-containing feedstock refers to one that contains methanol or is methanol, or the heated fuel contains propane or is propane. Say things. It is within the scope of the present disclosure that other processes for creating hydrogen gas from the hydrogen generating fluid 15 can be used additionally or alternatively. Similarly, other heated fuels and hydrogen generating fluids can be used. For example, the fluid 15 may include up to 25 parts by weight water or more in addition to methanol or other water-soluble carbon-containing feedstock. As another example, the combustible fuel may be a liquid when transported to the heating assembly and / or removed from the feed transport system. In FIG. 12, the hydrogen generating fluid and heated fuel are illustrated as being transported to the hydrogen generating region and heating assembly via fluid conduits 85 and 79, respectively. It is within the scope of the present disclosure that any suitable number and configuration of such conduits can be utilized. As described, in some embodiments, it may be preferable to conduct heat in the conduit to the heated discharge stream, such as preheating the fluid contained in the conduit. In FIG. 12, the valve assembly 60 is shown to include valves 61 and 63 that are configured to selectively restrict or permit the flow of heated fuel and hydrogen generating fluid. This structure is not necessary for all embodiments. When valves and / or valve assemblies are present, they may be configured manually by an operator or the like near the hydrogen generation assembly and / or automated or controlled to respond to input commands from the controller It may be constituted by the operated. The transport system schematically illustrated in FIG. 12 may include any suitable type and / or number of sources or feedstocks 112 that transport these streams, or may be in fluid communication. Good.

  In the example shown in FIG. 12, the heating assembly 60 takes the form of a burner 62 that combusts heated fuel with air to produce a heated discharge stream 66. The heating assembly 60 can utilize, for example, an igniter or any other suitable ignition source 89 described herein to initiate combustion of the heated fuel. It is also within the disclosure that the heating assembly includes a combustion catalyst instead of a burner.

  The heating assembly also generally accepts an air flow to assist in the combustion occurring within. The air flow can be transported through any suitable air delivery assembly, such as a blower, blower, compressor, etc. It is also within the scope of the present disclosure that air is taken from the environment in which the required heating assembly is used, without the air-driven pneumatic transport assembly. As a further variation, the stack and / or energy storage device can provide power to the air delivery assembly when the hydrogen generation assembly is coupled to the fuel cell stack and / or the energy storage device. In one example, the air stream 74 is mixed with the heated fuel feed stream 64 before entering the heating assembly. As shown, the air stream is mixed with the heated fuel 13 in the air entrainment zone 214 before entering the heating assembly. Additionally or alternatively, the supply air may enter the heating assembly 60 separately from the heated fuel.

  Also, heated discharge air 66 from the heating assembly is shown to heat the hydrogen generation fluid 15 as well as to heat the hydrogen generation region and before the fluid transported to the hydrogen generation region. If the heated fluid is a liquid stream when transported to the fuel processor, this liquid stream may be evaporated by a heated discharge stream from the heating assembly in the evaporation region 69. In FIG. 12, it can be seen that the evaporation region can be formed and / or located in any suitable configuration to provide the necessary heating (ie, exposure time) to the discharge stream to which it is heated. It is schematically illustrated as including a sinusoidal configuration for illustrative purposes. As shown, the sinusoidal region can be rotated 90 degrees generally from a horizontal configuration that can be used in some embodiments. Additionally or alternatively, at least a portion, if not all, of the hydrogen generating fluid is transported to the fuel processing system before being exposed to the heated discharge stream from the heating assembly. It is within the scope of the disclosure that it was previously a gaseous composition and / or has already evaporated.

  As illustrated in FIG. 12, the vaporized hydrogen production fluid stream is transported to a hydrogen production region 19 of the fuel processing system. In the example of the steam reforming apparatus shown in the figure, the reforming catalyst 23 in the hydrogen generation region generates a mixed gas stream 20 containing hydrogen gas and other gases, the main component of which is hydrogen gas, from the fluid 15. Any suitable reforming catalyst available from Sud Chemie, BASF, etc. can be used. The reforming catalyst can be placed in the hydrogen production region in any suitable form, such as a catalyst bed, as a coating for the structure in this region, such as pellets, powder, and the like.

  As also shown in FIG. 12, the fuel processing system includes a separation region 24 (which may be referred to as a purification region, as described) that receives a mixed gas or reformate stream 20 from a hydrogen production region. Including. As shown, the separation region 24 is a byproduct stream 28 formed from a portion of the mixed gas stream that permeates at least one hydrogen selective membrane and a portion of the mixed gas stream that does not permeate at least one hydrogen selective membrane. For the product hydrogen stream 14 formed from these parts, at least a hydrogen-selective membrane 30 is included. A schematic example of a fuel processing assembly including a plurality of separation regions 24 and / or a plurality of mechanisms for removing impurities from the generated hydrogen gas is also shown in FIG. A second separation region 24 that includes a methanation catalyst 32 that is configured to reduce the concentration of any carbon monoxide in the product hydrogen stream is shown in dashed lines. This second separation region may be referred to as a methane production region.

  When the byproduct stream has sufficient fuel value to be used as the fuel stream for the heating assembly 60, at least a portion of the byproduct stream can be transported to the heating assembly for consumption as a fuel stream. This is illustrated in the example shown in FIG. 12 where the fluid conduit 77 is configured to transport a byproduct stream 28 that is used as a combustible fuel in the heating assembly 60. As described, it is within the scope of the present disclosure that the fuel requirements of all heating assemblies to maintain the hydrogen production region in the appropriate temperature range for the product hydrogen gas can be provided by the byproduct stream. is there. In some embodiments, it may be preferred to include some of the produced hydrogen gas in the byproduct stream to increase the fuel value of the byproduct stream. This mixes some of the product hydrogen stream with the by-product stream and transports some of the product hydrogen stream independently to the heating assembly, leaving a sufficient amount of hydrogen gas in the by-product stream. This can be achieved by an exemplary mechanism such as designing the region. This can reduce the overall efficiency of the hydrogen production zone, i.e. the amount of hydrogen gas obtained per unit of hydrogen production fluid, while a separate fuel stream is supplied to the heating assembly during operation of the hydrogen production zone. Since it is not necessary, it may be suitable for some applications. Instead, when hydrogen gas is generated, some of the hydrogen gas and by-products generated from this reaction are transported to the heating assembly to maintain the hydrogen generation region in the desired temperature range. In embodiments where the fuel processor does not include a separation region, this configuration is still achieved by diverting or otherwise transporting some of the product hydrogen stream to the heating assembly to consume as combustible fuel stream.

  In the example shown in FIG. 12, the hydrogen generation assembly 10 includes an optional filter 230 through which the byproduct stream passes before being consumed as a fuel stream in the heating assembly. An optional flow restriction orifice 232 is also shown. Orifice 232 is configured to generate back pressure on the hydrogen generation assembly by restricting the flow rate of byproduct stream 28 that may pass therethrough. As described in further detail herein, the orifice 232 is against an idle operating condition that produces little or no hydrogen gas, a shut-off operating condition where the flow of the hydrogen generating stream to the fuel processing system is stopped. It may be useful to save fluid 15 when the demand for product hydrogen stream 14 is low while still maintaining the fuel processing system in a hydrogen production state, or in an active state.

  For example, the hydrogen generation fluid 15 may be transported to the hydrogen generation region 19 at a pressure in the range of 50-250 psi. This pressure releases the hydrogen production fluid from the feed transport system (including but not limited to the pressure vessel 59 described or any other pressurized source 499 used in certain embodiments). It can be determined at least in part by the pressure. Due to (at least in part) the pressure driven separation process described in at least one example, the pressure of the byproduct stream 28 and the product hydrogen stream 14 is less than the delivery pressure. When there is a demand for hydrogen gas produced by the hydrogen production assembly, the hydrogen gas is withdrawn from the fuel processing system separated from the mixed gas stream. Similarly, the byproduct stream is also drawn from the fuel processing system. Some back pressure on the byproduct stream may cause more hydrogen gas to be generated in the hydrogen selective membrane than can be generated if the orifice 232 is not carrying the byproduct stream and thereby the back pressure on the remaining fuel processing system. The separation that occurs in the separation region can be increased.

  If the demand for the product hydrogen stream 14 is less, the flow rate of hydrogen gas in this stream can be regulated or stopped via a suitable valve assembly or other flow control device such as included downstream of the separation region 24. Can even be done. At this time, a larger partial pressure of hydrogen gas is generated on the permeation side of the hydrogen selective membrane, and thereby hydrogen gas permeating the membrane can be suppressed. This in turn results in a greater overall flow rate of more hydrogen gas and byproduct stream 28. Without constraining or otherwise limiting the flow rate of this flow, it simply goes to the heating assembly or other destination. This cannot negatively affect the operation of the system, but can be wasteful from a hydrogen generating fluid perspective. In some embodiments, the burner assembly is consuming more fuel and / or fuel having a greater heating value so that an increased stream of by-product stream 28 and / or additional hydrogen in this stream. Depending on the minute, the overall temperature of the hydrogen production zone can be increased. If the by-product stream 28 has a sufficiently high flow rate, the flow rate may be flooded or otherwise impair the operation of the burner. It is within the scope of the present disclosure to include bypass valves, outlets, and other structures to selectively bypass some by-product streams so that they are not transported when heating fuel to the burner assembly. It is. As described, this may not be a concern in some embodiments, such as when the byproduct stream is not consumed as heated fuel in a heating assembly for a fuel processing system.

  By applying back pressure to the system through the orifice 232 or other suitable structure, the back pressure while the flow rate of the product hydrogen stream is regulated or stopped, such as from a location downstream of the separation assembly, The flow of hydrogen production fluid from the feed transport system can be constrained rather than flow. A potential advantage of using the orifice 232 is that the presence of the orifice is complex and typically allows the operation of the hydrogen generation assembly to be automatically performed without a motorized controller or sensor and / or associated structure. To be regulated or stabilized. Filter 230 and / or orifice 232 are not required, but can be used with any hydrogen generation assembly described, illustrated, and / or incorporated herein.

  During startup of the hydrogen generation assembly, the heated fuel 13 is first transported to the heating assembly, where it is ignited by any suitable mechanism for generating the discharge stream 66. This discharge stream 66 is then used to heat to an appropriate temperature (ie, at least the minimum hydrogen production temperature) for producing hydrogen gas from at least the particular fluid 15 utilized in the hydrogen production region. In an embodiment of the hydrogen generation assembly 10 that utilizes a controller, the controller may be configured to detect whether fuel ignition has begun. Any suitable sensor can be used for this detection. Illustrative non-limiting examples of this sensor include optical and thermal sensors such as thermocouples. If ignition does not occur, the controller may cause the fuel and / or fluid flow by the feed transport system (eg, by closing valves 41 and 43, stopping pumps used to propel the fuel / fluid, etc.). Can be configured to stop.

  Once the hydrogen production region is sufficiently preheated, the flow of heated fuel can be stopped and the flow of hydrogen production fluid can be initiated. This transition may include a short period during which neither fuel 13 or fluid 15 is transported to the hydrogen generation region or heating assembly (but is not required) or such a period may not occur. . For example, the flow of fuel 13 may be stopped when the flow of fluid 15 begins, or there is a period during which fuel 13 is transported to heating assembly 60 and hydrogen generating fluid is transported to hydrogen generating region 19. May be. In one example, the reactants utilized in the hydrogen production region 19 can be transported in stream 64. However, it is within the scope of the present disclosure for the hydrogen production zone to accept at least one added reactant or other fluid stream. An advantage of all reactants being transported in stream 64 is that these reactants can be heated as a unit at the same pressure and do not require a separate transport system or mechanism.

  As described and not required for all embodiments, the hydrogen generation assembly 10 and / or the energy generation system 42 incorporating the same may minimize the balance of plant power, if any. Insofar, it is within the scope of the present disclosure that it can be constructed. This means that the system can be implemented without the need for many of the fluid transport devices, controllers and other electronic devices conventionally utilized for these assemblies and / or systems. As described, even in embodiments where one of these fluids is a liquid when dispensed from the feed transport system, the heated fuel and hydrogen generating fluid can be stored under pressure. For example, the hydrogen production fluid may be alcohol, liquid hydrocarbon and / or liquid alcohol or a mixture of hydrocarbon and water. Conventional pumps and / or compressors have been used to draw from the feed from the feed and transport to the hydrogen production zone under suitable pressure, but are described, illustrated and / or incorporated herein. The feed transport system (though not required) draws and transports the hydrogen generation fluid to the heating assembly of the hydrogen generation assembly and to the hydrogen generation region of the assembly without the need for these pumps or compressors Can be configured. Furthermore, the fuel and fluid may be contained in common in the fuel container and can still be used for separate transportation. The integration of fuel and fluid to the same pressure can increase the compactness and / or portability of the system. An exemplary, non-limiting embodiment of a feed transport system that utilizes such containers or pressurized containers is described in connection with FIGS. 30-35.

  As described, it is disclosed that the flow of the heated fuel and hydrogen generating fluid can be controlled by the valve assembly, such as when the heated fuel and hydrogen generating fluid are stored or available under pressure. Is within the range. As an example, this flow may be controlled by a valve assembly 60 that may include two valves or three-way valves or other valves that provide at least three flow structures. Accordingly, in response to a first user input that initiates the flow of heating the fuel to the burner assembly, the heated fluid flow is initiated or the ignition source is activated and the hydrogen generation region begins to be preheated.

  This activation of the ignition source may be incorporated into the operation of the valve assembly to automatically respond to the operation of the valve assembly as needed, or may be initiated individually by an operator or the like. Ignition can be manually activated by the user or the like when the flow of heated fuel is initiated. It is also within the scope of the present disclosure that the ignition source is configured to automatically ignite upon receipt of the heated fuel stream, such that the ignition source includes a combustion catalyst. As a further example, the ignition source may be a switch used to initiate the flow of heated fuel to the heating assembly so that the ignition source is activated when the heated fuel flow is initiated or within a selected period thereafter. It may be incorporated so as to be operable. As a further illustrative, non-limiting example, when the system includes a battery 52 or other energy storage device (eg, a condenser, ultracapacitor, or flywheel), the device has sufficient time to begin burning the heated fuel. It can be used to supply power to the ignition source.

  For the steam reforming reaction utilizing a hydrogen production fluid comprising methanol and water, the hydrogen production zone is preferably heated to at least 300 ° C. One example of a preheat temperature threshold is: 300 ° C, 325 ° C, 350 ° C, 375 ° C, 400 ° C, a temperature of at least 350 ° C, a temperature in the range of 350-450 ° C, a temperature in the range of 350-400 ° C, Includes temperatures in the range of 375-425 ° C. The desired threshold temperature for detection when the hydrogen production fluid flow is initiated is the mechanism by which hydrogen gas is produced, whether the heating assembly continues to supply heated fuel after the hydrogen production fluid flow is initiated, the heating assembly Depending on factors such as the rate and / or duration of this supply of heated fuel to the fuel, the composition of the hydrogen generating fluid, the environment in which the hydrogen generating assembly is used, user preferences, and the like.

  Determining that the hydrogen production region has been heated to the selected threshold temperature can be accomplished via any suitable mechanism and / or method. For example, a temperature sensor can be used to indicate the temperature of the hydrogen production region. The operator may manually detect the temperature if it is within an acceptable temperature range, and may initiate and / or heat the flow of hydrogen generating fluid to the hydrogen generating region, such as by simply operating valve assembly 60. Heated fuel flow to the assembly may be stopped or reduced. In order to automatically start the hydrogen generating fluid flow and / or reduce or stop the flow of heated fuel when a preselected threshold temperature is detected, the temperature sensor may include an appropriate temperature driven solenoid or actuator. It is also within the scope of the present disclosure to be coupled to the valve assembly, such as through. For example, bimetallic temperature sensors, solenoids or other detectors or actuators can be utilized.

  As long as the heated fuel, operating environment or other parameters do not change, the time required to preheat the hydrogen production zone must be reproducible. Thus, for this threshold time corresponding to a predetermined period during which the hydrogen production region is preheated to an allowable temperature, a timer can be used to indicate when the allowable time has elapsed. The timer can be configured to provide a visual, audible, or other signal to the operator. It is also within the scope of the disclosure that a timer is coupled to the valve assembly to automatically start the hydrogen generating fluid flow and / or stop or reduce the flow of heated fuel at the expiration of the preselected period. It is.

  The hydrogen production zone is configured to operate and is subjected to steam reforming or other mechanism that initiates the flow of hydrogen production fluid to the hydrogen production zone, to a temperature suitable for providing hydrogen gas. When is heated, hydrogen gas begins to be generated in the hydrogen generation region in response to the transport of the fluid 15. As will be described, it is within the scope of the present disclosure that this can occur with two or fewer actuations of the valve assembly and with the actuation of any ignition source. The by-product stream produced in the separation zone 24 can be configured to have a fuel value sufficient to provide heated fuel for the heating assembly when the hydrogen producing assembly produces a produced hydrogen stream. Thus, as long as the supply of hydrogen generating fluid is not exhausted, the assembly may be autonomous within the appropriate operating temperature range. Since the lack of hydrogen product fluid flow means that there is no product hydrogen vapor or byproduct stream 28 flow, the system should be configured to shut down automatically.

  When the hydrogen generation assembly 10 is coupled to a fuel cell stack to provide an energy generation system 42, the stack is automated during transport of the generated hydrogen stream 14 and the air stream 74 or other oxidant stream to the fuel cell stack. Can be configured to generate current. The hydrogen gas flow to the stack occurs generally a few seconds after the fluid 15 flow to the preheated fuel processing system is initiated. Air flow is automatically transported to the fuel cell stack, such as when the stack includes an open cathode structure where air is automatically drawn from the environment where it is used without the need for a fan, blower or compressor. Can be configured. In such embodiments, the energy generation system may automatically generate this current and / or operate energy consuming equipment (which may be electronically connected to and / or integrated with the energy generation system 42). It only provides power while requiring minimal operator input and / or the above. In some embodiments, for an initial supply of air provided by an operator, the fuel cell stack may include an electrically driven fan or blower that is driven by the fuel cell stack. As a further variation, this initial supply may be provided by a fan or other blower driven by a battery or other energy storage device. At the time of generating the current of the fuel cell stack, the battery or other energy storage device is no longer needed because the stack can meet the power requirements of this type of pneumatic transport system. When the electrical ignition source and / or time is utilized in the heating assembly and / or the hydrogen generation assembly, the battery or other energy storage device can also provide power to them. In experiments, the energy requirements of these devices are very small and tend to be short-lived, which are not essential for all embodiments.

  Exemplary non-limiting embodiments in a fuel processing assembly 31 configured to produce a product hydrogen stream 14 and a hydrogen production assembly 10 including the same are described with respect to FIGS. In the following description, the hydrogen production fluid 15 is described as a mixture of methanol and water. However, it is within the scope of the present disclosure that any of the carbon-containing feedstock 18 and / or hydrogen generating fluid composition described and / or incorporated herein can be utilized. The following example provides a non-limiting example shown in a feed transport system configured to transport liquid and gaseous fuel streams to a corresponding heating assembly. The examples shown are for the purpose of illustrating examples of suitable structures and are not intended to require the same or to limit the scope of the present disclosure.

  Returning briefly to FIG. 12, the illustrated example that may be performed by any of the shells 27, feedstock transport systems, etc. described, illustrated and / or incorporated herein is a heating assembly. May be configured to receive a byproduct stream from the fuel processor and burn. In some embodiments, the by-product stream may have sufficient fuel value to transition to a hydrogen production operating state after at least activation of the hydrogen production assembly and be utilized as the only source of heated fuel. . In some embodiments, it may even be preferred to configure the fuel processor to include sufficient residual hydrogen gas to achieve this optional objective. A potential trade-off associated with reducing the amount of hydrogen gas present in stream 14 is that a continuous flow of fuel 13 is pumped to maintain the hydrogen production region at a suitable hydrogen production temperature, such as within the preferred hydrogen production temperature range. There is no need to be done or else it needs to be transported to the heating assembly and consumed.

  When the gaseous fuel 13 is utilized during startup of the hydrogen generation assembly, and when the byproduct stream 28 is utilized as fuel for the heating assembly 60 when the hydrogen generation assembly is in a hydrogen generation operating state, the gas stream is , May be exposed to an ignition source (or an existing flame) and may be positioned relative to the hydrogen generation region via any suitable mechanism and / or structure. An example of a suitable non-limiting configuration shown is to define a generally parallel flow path for each gas flow and / or position each gas flow in a suitable position relative to the hydrogen generation region. The gas flow is made to flow through a nested burner assembly that builds a flow path. FIG. 13 shows an example of a heating assembly 60 that includes a burner assembly 282 configured to define a first fluid conduit 284 for the gaseous combustible fuel 13 and a second fluid conduit 286 for the byproduct stream 28. . The first fluid conduit may additionally or alternatively be described as an activation burner assembly, and the second fluid conduit may additionally or alternatively be a main or main burner assembly. Can be described. As shown, the main and activation burner assemblies define separate gas flow paths for the combustible flow contained therein until after the ignition of these flows. FIG. 13 also illustrates an example of a suitable burner structure that may be used in the heating assembly 60. The example shown demonstrates that in some embodiments it may be preferred to utilize a burner assembly that includes separate flow paths for the heated fuel 82 and the byproduct stream 28. Various elongated (ribbon) and point-sized orifices are shown to burn with air with fuel and / or by-product streams flowing through them.

  14 and 15 include a hydrogen generation region, a separation region, and a burner assembly in a common shell or housing 68 that is open to the environment in the fuel processing system 31 so that air can be circulated by the housing. Is shown. As perhaps best shown in FIG. 14, an example of the housing 68 includes spaced apart supports 260, generally designated 240, that support the body region 62 of the housing above the surface on which the mount is located. . The housing further includes an outlet port for the product hydrogen stream 14 and an inlet port for the fuel stream 16 of the hydrogen product fluid 15 and the fuel stream 64 of the combustible fuel 13. As schematically illustrated in the dashed line in FIG. 15, the shell may include an insulating layer 242 to reduce the external temperature of the system. Also shown is an inlet 244 for the air stream 74 for the heating assembly and an outlet 246 for the heated discharge stream 66 from the heating assembly. In the illustrated example, the outlet for the heated discharge stream is covered by a heating plate or shroud 248. Although not required, it is within the scope of the present disclosure to load or otherwise place at least some feed transport system, such as a fuel or fluid supply on plate 248. During use of the fuel processing assembly, the heated discharge stream heats a member (or other object to be heated) of the feed transport system disposed on the plate. The plate 248 may have any suitable configuration that facilitates positioning and / or fixing of the object being heated on the plate and may include a mount or other receiver that facilitates positioning. .

  As shown in FIG. 15, the shell provides an outer surface of the shell by providing a jacket or cooling passage 252 through which the airflow flows before it is used to preheat the airflow and assist combustion in the heating assembly. A flow path 250 is defined for the air flow 74 that cools the air. As perhaps best shown in FIG. 15, the air flow flows through passage 252 and then through inlet 254, the central region or compartment of the shell in which the hydrogen generation region, separation region and burner assembly are housed. 256 flows. FIG. 15 also shows an example of a fuel processing assembly that includes a heating assembly having a burner assembly 282.

  As described, some feed transport systems 22 for hydrogen generation assemblies according to the present disclosure are configured to transport a stream of liquid combustible fuel 13 to a heating assembly. Some liquid combustible fuel streams cannot be ignited immediately and / or cannot be burned at a particular operating temperature where a hydrogen generation assembly can be utilized. As a non-limiting example, the fuel stream can be transported to the heating assembly as a liquid fuel stream at a temperature in the range of approximately 25 ° C. to approximately 100 ° C., but temperatures above or below this exemplary range may be It can be used within the scope of the disclosure. As used herein, “liquid” or “liquid phase” is an operating parameter when a fuel stream is transported to a heating assembly, with little or no fuel in the liquid phase. Is also meant to indicate a fuel stream comprising at least a majority. In addition, when the fuel stream 64 includes a carbon-containing feedstock 18 or a synthetic stream comprising carbon-containing feedstock and water (eg, a synthetic stream 90 described below), the fuel stream transported to the heating assembly 60 is: It may be in the liquid phase with the operating parameters being transported to the heating assembly. The operating parameters described above are not intended to be exclusive examples. Instead, these parameters represent examples of typical parameters, and parameters outside these ranges are still within the scope of the disclosure. In many applications, such as a heating assembly incorporated in a fuel processing assembly used for portable or mobile applications, the operating parameters for transport of the fuel stream 64 depend on the environmental conditions in which the fuel processing assembly is used. Can vary widely. For example, the fuel processing assembly may transport the fuel stream 64 to the heating assembly 60 at a temperature in the range of less than 0 ° C. to greater than 100 ° C.

  Other temperature ranges in the illustrated non-limiting example of a fuel processing assembly that can be used are less than 30 ° C, less than 20 ° C, less than 10 ° C, less than -10 ° C, less than -20 ° C, less than -30 ° C,- Temperatures below 40 ° C, temperatures in the range of -50 ° C to 100 ° C, temperatures in the range of -50 ° C to 50 ° C, temperatures in the range of -50 ° C to 30 ° C, temperatures in the range of -30 ° C to 50 ° C, And the temperature of the range of -30 degreeC and 30 degreeC is included. As described, during startup of the fuel processing assembly, the heating assembly is configured to receive a liquid fuel stream and initiate combustion. Some liquid fuels do not become liquid in the exemplary temperature range described above, and therefore the composition of the liquid fuel used can be selected by factors such as the ambient temperature expected around the fuel processing assembly. For example, methanol is not a liquid at 100 ° C.

  In FIG. 16, an illustrative, non-limiting example of a hydrogen generation assembly 10 that includes a heating assembly 60 that is configured to receive a liquid fuel stream 64 is schematically illustrated. The heating assembly 60 includes a burner assembly 62 and may include associated inlets, outlets, and other mechanisms that are compatible and consistent with the heating assemblies provided herein. As schematically shown in FIG. 16, a burner assembly 62 according to the present disclosure includes an activation burner assembly 356 and may include a main or main burner assembly 358 in some embodiments. Literally, the activation burner assembly is configured to heat at least the hydrogen generation region of the fuel processor to an appropriate hydrogen generation temperature. The main or main burner is configured to continue to provide at least heating to the hydrogen generation region during the fuel processor hydrogen generation operation. The main burner can be configured to consume a gaseous fuel stream. This gaseous fuel stream is partly or completely formed from a part of the mixed gas stream produced by the hydrogen production region. In certain embodiments in which both the activation and primary burner assemblies are present, these assemblies may be separate assemblies and / or may share one or more members. Within the scope of the disclosure.

  The heating assembly 60 shown in FIG. 16 is in heat transfer with the hydrogen generation region 19 of the fuel processing assembly and is thereby configured to heat or otherwise include a reforming region. Can be configured to heat a portion of the. As described above and as shown in FIG. 16, the heating assembly 60 may be disposed within the shell 68 of the fuel processor 12. However, it is within the scope of the present disclosure that it may be located at least partially or completely outside the shell. Appropriate conduits, conductive materials, and other devices may be provided to transfer the thermal energy of the combustion discharge stream 66 to the hydrogen generation region of the fuel processing assembly.

  As schematically illustrated in FIG. 16, the heating assembly 60 includes at least one fuel chamber 376 and an ignition source 89 in the form of at least one heated ignition source 378 and is configured to receive at least one air stream 74. Has been. In FIG. 16, the fuel chamber 376 is shown to include a bottom 392 and sidewalls 394. The fuel chamber 376 includes a top 395, which may be fully or partially open top, thereby forming an open retainer for holding the liquid fuel being transported. . In such embodiments, the air flow 74 can be transported (by a blower, fan or other suitable device) and / or from the ambient environment via the open top 395 to the fuel chamber 376. And can flow naturally.

  As illustrated in FIG. 16, the hydrogen generation region 19 or other portion of the fuel processing assembly heated by the combustion discharge stream 66 is generally located above, often relatively close to, the top of the fuel chamber opening. To do. This allows the combustion stream to heat this structure as the combustion stream naturally flows from the fuel chamber. As described, blowers, fans, and other suitable structures may be added to facilitate the transfer of the heated combustion stream to the reforming region 19 and / or other regions of the fuel processing assembly. Or alternatively may be used.

  In some embodiments, the fuel chamber 376 may include a complete or partial top member 404 to fully or partially surround the fuel chamber. When the fuel chamber 376 includes a complete or closed top member to form a substantially closed combustion chamber, the fuel chamber 376 may supply air for combustion, such as air stream 74 described above, to the fuel chamber. One or more air inlets 399 can be included as well as one or more outlets. The air inlet and discharge port may be configured for natural air flow or may be connected to a pump, blower, compressor, valve or other equipment for controlled or pressurized fluid flow. The inlet port 399 for the air flow 74 is shown in a dashed line in FIG. 16 to visually represent that the (at least partly) open top fuel chamber may also include one or more inlet and / or outlet ports. Can be shown. A heating assembly having a closed top 395 can provide more radiant heat than a comparable open top heating assembly, by using one or more discharge ports (and associated fluid conduits extending therefrom). The combustion discharge stream 66 may be configured to be transported to one or more selected areas or structures of the fuel processing assembly. Such areas then include areas that are more difficult to optimally heat only by convection of the discharge flow heated by the opening top of the fuel chamber.

  At least one fuel chamber is configured to receive at least a portion of the fuel stream 64 and includes combustible fuel (13) according to the present disclosure. The fuel stream 64 may contain additional components such as water, air, oxygen, hydrogen, or other components necessary for combustion, such as flammability, non-flammability, and / or air, for example. Feedstock 18 is included. Although a single fuel stream 64 is shown in FIG. 16, multiple fuel streams 64 may be used, and additional streams may include the same or different carbon-containing feedstocks, other combustible fuels, It is within the scope of the present disclosure that air or other components can be supplied. In addition, as described above, the fuel stream 64 may include a liquid, carbon-containing feedstock that is the same carbon-containing feedstock that is transported to the fuel processor 12. Similarly, the fuel stream 64 includes a carbon-containing feedstock and water and includes a composite stream that may have the same or essentially the same composition as the feed stream for the hydrogen generation region 19 of the fuel processor. But you can.

  The heating assembly 60 shown in FIG. 16 includes an ignition source in the form of a heated ignition source 378. The ignition source 378 is configured to heat the carbon-containing feedstock 18 of the fuel stream 64 and start combustion. The thermal ignition source 378 may be located or otherwise located outside the fuel chamber 376, as indicated by the solid line, and may be located or located within the fuel chamber 376, as indicated by the dashed line, or , Partially outside the fuel chamber 376, and partially inside the fuel chamber 376. The heating and ignition source 378 may include any suitable structure or device for heating and igniting the fuel stream in the presence of air to initiate its combustion. In some embodiments, the thermal ignition source 378 may include a plurality of devices.

  Examples of suitable heating and ignition sources 378 include at least one of spark plugs, glow plugs, pilot lights, combustion catalysts, glow plugs coupled to the combustion catalysts, electrically heated ceramic igniters, and the like. In some embodiments, the heat ignition source 378 also includes an electrical resistance heating element, either alone or coupled with an igniter (eg, a spark plug). A glow plug is an example of an electrical resistance heating element that can be used alone to heat and ignite a carbon-containing fuel received by a fuel chamber. The heating and ignition source 378 may include an electrical resistance heating element configured to be heated to a temperature that is sufficiently hot to ignite the carbon-containing fuel in the fuel chamber 376, also referred to as red or incandescent temperature.

  FIG. 17 schematically illustrates that the heating assembly 60 includes an ignition region 380 and a combustion region 382 such that the ignition region can be located closer to the ignition source than the combustion region. In such an embodiment, the carbon-containing fuel disposed in the fuel chamber can be mixed with air in the ignition region 380 and ignited to be combusted to produce a heated combustion stream 66; This combustion stream may be discharged from the heating assembly 60 to heat at least the reforming region of the fuel processor 12. It is within the scope of the present disclosure that combustion initiated in the ignition region 380 can spread elsewhere in the heating assembly 60 and / or the hydrogen generation assembly 10. For example, the combustion may remain in the ignition region, and after ignition, may extend to the combustion region 382 so that combustion occurs in the combustion region and the ignition region. In addition, due to the dispersion of fuel vapor, combustion can occur in other parts of the fuel processing assembly. As used herein, the ignition region 380 is used to refer to an area or region in the fuel chamber 376 that is smaller than the entire fuel chamber. That is, the ignition region 380 is a subset of the fuel chamber that can be physically defined or can be a region of the fuel chamber, such as a particular end region, corner region, or the like.

  As indicated by the solid line in FIG. 16, the fuel stream 64 is fed into the fuel chamber until it is consumed to assist combustion in the fuel chamber, as described in further detail herein. At least a substantial portion of what remains (if not all) can be transported as a bulk liquid. The fuel stream 64 may be transported to the fuel chamber opening or fill port via a suitable fluid conduit. The liquid fuel then flows in the fuel chamber under the force of gravity, adsorption / wicking force applied by any structure, such as in the fuel chamber. It is within the scope of the present disclosure that the heating assembly can include at least one or more distribution conduits that extend into the fuel chamber and through which the liquid fuel stream flows before being dispensed in the fuel chamber. . The distribution conduit may include an opening or other outlet along its length, may include an outlet (in its end or in the fuel chamber), and / or further liquid fuel flow in the fuel chamber. One or more branches may be included to distribute. Although not required for all embodiments, the distribution conduit is a liquid fuel below or adjacent to the heated ignition source to distribute the liquid fuel stream to one or more selected areas, such as a fuel chamber, in use. It may be configured to selectively transport at least a portion of the stream. As described herein in connection with FIG. 17, when the fuel chamber includes a transport medium, the distribution conduit may be configured to transport the liquid fuel from the conduit before flowing into the fuel chamber. Can be used (although not required) to distribute the liquid fuel stream through at least a portion of

  In operation, and as described above, the fuel stream 64 can be transported to the heating assembly 60 as a liquid or at least partially in a liquid phase. The fuel stream 64 may be transported to a fuel chamber 376 under an operating or transport condition that includes a first temperature and a first pressure. The carbon-containing feed or feeds that are transported to the fuel chamber may have a flash point or minimum ignition temperature that is higher than the first temperature at which the carbon-containing feed or feeds are transported to the fuel chamber. . As used herein, “flash point” refers to the lowest temperature at which the vapor pressure of a liquid is sufficient to form an ignitable mixture with air near the surface of the liquid. The flash point for the fuel stream received by the fuel chamber 376 depends on factors such as the carbon-containing feedstock in the fuel stream, the relative concentrations of the carbon-containing feedstock and other components in the fuel stream, the fuel chamber conditions, etc. Can be determined.

  While the flash point indicates the lowest temperature at which the liquid fuel can have sufficient vapor pressure above the surface to form an ignitable mixture with air, whether or not the mixture ignites depends on the location of the ignition source. Depends on the concentration of combustible fuel vapor in the air. For example, if the ignition source is spaced from the surface of the liquid carbon-containing feedstock, the concentration of combustible fuel vapor can be diluted by a number of factors. Lower flammability limits are often used to indicate the minimum concentration of combustible fuel vapor in the air that the flame can propagate through. As used herein, “ignition vapor pressure” can be used to indicate the minimum vapor pressure at which fuel ignition occurs in air.

  The temperature of the liquid carbon-containing feedstock in the fuel chamber 376 required to provide an ignitable vapor concentration (ie, a concentration at least equal to the lower flammability limit) may be higher than the flash point temperature, Is called the ignition temperature. While the ignition temperature is due to environmental factors such as the availability of fresh air in the vapor space above the liquid fuel in the area adjacent to the ignition source and the ability of the fuel vapor to be released into the fuel chamber, the ignition temperature Temperature is referred to herein as a characteristic of a carbon-containing fuel.

  The fuel stream may enter the fuel chamber at a first temperature and have an ignition temperature that is greater than the first temperature. In some embodiments, the carbon-containing fuel that is transported to the fuel chamber may have an ignition partial pressure, and the carbon-containing fuel in the fuel chamber may have an initial partial pressure that is less than the ignition partial pressure. In some applications of the heating assembly 60, the first temperature (transport temperature) of the fuel stream 64 may be such that there is substantially no carbon-containing feedstock in the vapor phase. In other applications, the fuel stream may be transported at a first temperature where some carbon-containing feedstock is in the vapor phase. However, for many applications, the concentration of the vapor phase carbon-containing feedstock at the first temperature is not sufficient to form a combustible mixture at the location of the heated ignition source 378. That is, the first temperature is lower than the ignition temperature of the carbon-containing fuel. Applications and configurations in cold air where the fuel stream 64 includes a synthetic stream having water and a carbon-containing feedstock are sufficiently high in feed steam or fuel steam containing carbon to form an ignitable mix with a heated ignition source Typical, but not exclusive, concentrations are not obtained at the first temperature.

  With continued reference to FIG. 16, the fuel chamber 376 may be described as including a liquid fuel region 396 and a fuel vapor region 398. As shown, fuel chamber 376 is an open vessel and fuel vapor region 398 is defined by the liquid fuel surface of liquid fuel region 396 and by side wall 394 of fuel chamber 376 but open at the top. (Ie, theoretically, the fuel vapor region extends as long as the fuel vapor can dissipate within the fuel processing assembly). In embodiments where the fuel chamber 376 includes a top member, it may be described that the fuel vapor region 398 is at least partially constrained to the top by a whole or partial top member, whether in whole or in part.

  As briefly described above, the heating assembly 60 includes a heating ignition source 378. As shown in FIG. 16, the heating and ignition source 378 takes the form of an electrical resistance heating element 400 that is completely disposed in the fuel vapor region 398. As shown, the thermal ignition source is illustrated as being located above the liquid fuel region of the fuel chamber. However, it is within the scope of the present disclosure that at least a portion of the thermal ignition source is disposed in the liquid fuel region 396, as illustrated by the dashed line in FIG. Similarly, other functionally suitable structures can be used for the heating and ignition source 378 with electrical resistance heating elements, and the illustrated wound configuration is merely illustrated. It is within the scope of the present disclosure to be only examples. Although a heating and ignition source 378 is shown adjacent to one end of the heating assembly 60, the heating that allows at least a portion of the heating and ignition source 378 to be in sufficient contact with the fuel vapor to ignite the carbon-containing fuel in the fuel chamber. It is within the scope of the present disclosure that the thermal ignition source 378 can be located anywhere in the assembly 60. As a non-limiting example shown, the heating and ignition source can be disposed along a lateral wall of the fuel chamber, can be disposed in a peripheral region of the fuel chamber, or can be disposed in a central region such as the fuel chamber. .

  With continued reference to FIG. 16, the thermal ignition source 378 is shown in a wound configuration and as an integral piece of equipment. Other configurations are within the scope of the present disclosure. For example, the unitary heating and ignition source 378 may be linear, may include a linear portion and a curved portion, or otherwise wound, bent, or other shape Or it can be configured in configuration. Additionally or alternatively, the thermal ignition source 378 may include a plurality of devices, such as 2, 3 or more members. For example, the second device can be configured to provide an ignition source while the first device can be configured to heat the liquid carbon-containing fuel in the fuel chamber. The ignition source may be a spark plug or other intermittently or selectively actuated ignition source, or a glow that provides a red hot surface at a temperature sufficient to ignite the fuel vapor in the fuel chamber. It may be a plug or other ignition source. As another example, two or more complete heating and ignition devices may be used, such as two or more spaced resistance heating elements.

  As described, the thermal ignition source 378 may include one or more devices. Regardless of its configuration, the heating and ignition source 378 may be understood to provide a heating region and an ignition region. The heating region and the ignition region may be separate portions of the heating and ignition source 378, may be the same portion, or may include overlapping portions. In an integral heating and ignition source that is completely disposed in the fuel vapor region, for example, the heating region and the ignition region may be in the same range. In a composite member heat ignition source, (at least primarily) one member may be configured to heat the liquid while (at least primarily) the other member may be configured to ignite the vapor. Additionally or alternatively, a unitary device may be composed of two or more different structural parts that provide different properties or characteristics as described herein, eg, different materials. One such part may be suitable for heating the liquid (i.e. composed primarily), while the other part may be suitable for igniting the fuel. In addition, a common structure integral heat ignition source or any other heat ignition source may be disposed in the first portion of the liquid fuel and the second portion of the fuel vapor. In this type of configuration, if the portion of the fuel vapor is in the ignition region, it may be considered as a heating source in some applications while the portion of liquid fuel may be considered as the heating region.

  As described above, the thermal ignition source 378 may comprise any number of equipment, structures, circuits, members and / or materials. In some embodiments, the thermal ignition source 378 can include an electrical resistance heating element 400. The electrical resistance heating element 400 may include a conventional wire formed of a suitable electrical resistance material that generates heat when subjected to an electrical current. Illustrated non-exclusive examples of this type of material include tungsten and nichrome alloys (eg, 80Ni20Cr and 60Ni16Cr24Fe). In addition, the material used in the electrical resistance heating element 400 has a high thermal breakdown temperature and is non-reactive with the carbon-containing fuel in the fuel chamber, and the performance in the fuel chamber condition, and Otherwise, it can be selected based on the performance in a suitable state that can affect the ability of the heating and ignition source to heat and ignite the fuel in the fuel chamber. Typical materials include silicon carbide and other refractory materials. It is within the scope of the present disclosure that any suitable material or combination of materials can be used in the thermal ignition source 378. The specific materials used in a given embodiment are the carbon-containing feedstock of the fuel stream, the hydrogen generation mechanism or mechanisms utilized by the fuel processor, the heating assembly and fuel chamber configuration, and the heating ignition source configuration. And other factors such as alignment.

  With continued reference to FIG. 16, the heating and ignition source 378 optionally includes a controller (eg, controller 88) configured to monitor and / or control the operation and / or operating conditions of the heating and ignition source. Shown as being connected and / or in communication. The controller 88 is at least one of turning on / off the heating ignition source, controlling the heating rate of the heating ignition source 378, and controlling its surface temperature over time, among other possible functions. It can be any suitable manual or automatic controller that is configured to do the following. The controller 88 may be disposed entirely within the heating assembly 60, may be partially disposed within the heating assembly 60 and partially disposed outside the heating assembly 60, or may be disposed entirely within the heating assembly 60. Although it may be arranged outside 60, it is in communication with a heating ignition source. In some embodiments, the controller 88 may be within the fuel processing assembly 31 but outside the heating assembly 60. It is also within the scope of the present disclosure that a controller 88 can be located outside the fuel processing assembly for more convenient user access during operation of the fuel processing assembly. In some embodiments, the controller 88 may include and / or communicate with a power source 103 (eg, battery 52) for a heated ignition source (such as to regulate power transport). The controller may be configured to perform other functions, and thus the controller 88 may be implemented as a part or functional component in a fuel processing assembly and / or controller for a fuel cell system in which a heating assembly is utilized. .

  As described, the heating assembly 60 (and / or the burner assembly 62) may include a main burner assembly 358 in addition to the activation burner assembly 356. In FIG. 18, the main burner assembly 358 is schematically illustrated and can be configured to receive a gaseous fuel stream. For example, the byproduct stream 28 can be transported to a heating assembly for use as a fuel for the main burner assembly. As described in more detail herein, when a primary burner assembly is present, this assembly can be positioned in various directions relative to the activation burner assembly. These illustrated locations include, but are not limited to, the location where the main burner assembly is housed within the startup burner assembly, the primary burner assembly being above the startup burner assembly (ie, in proximity to the hydrogen generation region). And the position where the burner assembly and the activation burner assembly are disposed at the same or similar distance with respect to the hydrogen production region. As illustrated in FIG. 18, byproduct streams are not transported to the heating assembly, other gas fuel streams are transported to the main burner assembly, the heating assembly does not include the main burner assembly, and / or Alternatively, it is also within the scope of the present disclosure that by-products (and / or other gaseous fuel streams) are transported to the startup burner assembly for combustion during the hydrogen generation operation of the fuel processing assembly.

  FIG. 17 illustrates another example of a hydrogen generation assembly 10 that includes a fuel processing assembly 31, a fuel processor 12, a hydrogen generation region 19, and a heating assembly 60, substantially as described above. These members are identified with reference numbers consistent with those previously described. It is within the scope of the present disclosure that any of the structures, elements and / or variations described and / or illustrated herein can be used by or in these members and the hydrogen generation assembly 10. . As shown, FIG. 17 provides another example of a heating assembly 60 that includes an activation burner assembly 356 and a main burner assembly 358. The heating assembly 60 also includes a fuel chamber 376 and a heated ignition source 378. The fuel chamber 376 is illustrated with a bottom 392, sidewalls 394, and a top member 404. The top member may be a partial top member, as shown, or it may be a complete top member as described above. As illustrated at 405, the top member 404 may include one or more vents, or air passages 405, through which air flow is drawn into the ignition steam and / or combustion region, although not necessarily. Or inflow.

  In addition, the fuel chamber 376 may optionally include at least one baffle 406 illustrated in dotted lines in FIG. The baffle may define a fuel vapor region and / or an ignition region 380 and a combustion region 382 at least partially or separately in cooperation with the top member. As described above, the ignition region 380 includes a region where initial ignition of fuel in the fuel chamber 376 occurs. The ignition region 380 and the combustion region are defined by an ignition region, which is a region where fuel vapor is ignited by a heating ignition source, and by a combustion region, which is an arbitrary region where fuel is burned by propagating a flame from the ignition region. Can be distinguished. In some embodiments, the ignition region 380 and the combustion region 382 can be spaced apart from each other. One example of this type of configuration is illustrated in FIG. 17 including an optional baffle 406 and top member 404. As shown, baffle 406 extends downwardly from top member 404 to form an ignition chamber 408 that is at least partially enclosed. A heating ignition source 378 is disposed in the ignition chamber 408 and, as described above, in the fuel vapor region therein, in the liquid fuel region therein, or in the liquid fuel region and the vapor fuel region. It may be partially arranged on both.

  The ignition chamber 408 may be configured to at least partially limit fuel vapor that evaporates from the liquid fuel as a heated ignition source that heats the fuel chamber. By at least partially limiting the fuel vapor, the ignition chamber 408 is heated (by reducing the dissipation of the fuel vapor and minimizing the possibility that the fuel vapor can be blown away from the heated ignition source by environmental conditions. It is possible to promote or support the start of fuel ignition. Otherwise, these factors can cause the actual ignition temperature or flash point to rise above the theoretical ignition temperature or flash point of a particular fuel composition. It is understood that when the fuel chamber 376 includes an ignition region 380 (eg, ignition chamber 408), the ignition region can communicate with the combustion region so that flames and combustion initiated in the ignition region can propagate to the combustion region. Is within the scope of the disclosure. This terminates above the surface of the liquid fuel region, thereby defining a flame passage 407 in which flame and combustion can propagate or in the remainder of the fuel chamber 376 from the ignition chamber 408. A baffle 406 is shown in FIG.

  Referring to FIGS. 16 and 17, the evaporation zone 69 is illustrated as the length of a tube 415 that extends generally between or between the heating assembly 60 and the hydrogen generation zone 19. In the illustrated example, the evaporation region (ie, tube 415) is configured to define a plurality of channels that extend generally in parallel with the heating assembly and the hydrogen generation region. This provides a relatively greater heat transfer effect than simply passing between the heating assembly and the hydrogen production region at once. The illustrated example also shows that the tube extends along a passage that is sinusoidal or other laterally extending under the hydrogen generation region. This tube also increases the heat transfer effect (ie, the time during which the feed stream is heated by the heated discharge stream before being transported to the hydrogen production zone). The shape, orientation, length, cross-sectional area in the evaporation region, the relative position to the hydrogen generation region and / or the heating assembly, the number of passages, etc. are examples that can vary within the scope of this disclosure. The illustrated example is intended. Regardless of its specific configuration, this region is a liquid feed used to produce hydrogen gas into the hydrogen generation region of the fuel processor and transport this stream as an evaporated feed stream to the hydrogen generation region. Must be designed to accept flow. This feed stream evaporates in the evaporation zone through heat exchange with at least the discharge stream from the heating assembly.

  The heating assembly 60 according to the present disclosure may be used in a fuel processing assembly that does not include an evaporation region for the feed stream for the hydrogen generation (reformation) region of the fuel processor and / or directly by the discharge stream 66. It may include an evaporation region that is not heated and / or not disposed between the heating assembly and region 19. An evaporation zone comprising at least one length of the tube, or another closed zone where the feed stream is evaporated by heat exchange with a heated discharge stream 66 from a heating assembly flowing outside the tube, or evaporated When configured with other regions through which the feed stream flows, the tube / region 415 provides a desired exposure time and a corresponding amount of heat transfer during the evaporation region for the feed stream prior to entering the fuel processor. It can be formed or designed in any configuration.

  FIG. 17 also illustrates that a fuel chamber 376 according to the present disclosure may include (but is not required) a transport medium 410 that is at least substantially disposed in the liquid fuel region of the fuel chamber 376. The transport medium 410 may be configured to draw the liquid fuel in the fuel chamber 376 into the top or top surface 412 of the transport medium for combustion. At least the top surface of the transport medium and any additional regions in the medium proximate to the top surface may extend to the surface of the liquid fuel region and / or outside thereof. Accordingly, the transport medium 410 may be configured to move (ie, transport or otherwise transport) liquid fuel from the fuel chamber to the top or top surface of the transport medium 412 and / or It can contain structures. Refractory materials and materials that are configured to tolerate the elevated temperature and specific chemical environment of the fuel chamber 376 may be utilized. For example, in some embodiments, the transport medium 410 can include a ceramic or glass material. When a solid block or ceramic or other absorbent material is used as the transport medium, this material is not essential, but it can be drilled or otherwise drilled into a plurality of holes or other openings formed in the material. May be included.

  In some embodiments, the transport medium 410 may be porous or otherwise configured to absorb liquid fuel into the fuel chamber 376. The absorbent material 422 in the transport medium 410 is liquid during transport in a fuel processing assembly having a fuel chamber that is not substantially closed, such as a fuel chamber configured as a reservoir that is at least substantially top open. The outflow of fuel can be prevented. The absorbent material may be configured to draw liquid fuel and move the liquid fuel toward the upper portion 412 as the liquid fuel is consumed. When the transport medium 410 is configured to absorb the least amount of liquid fuel that is transported to the fuel chamber, the liquid fuel that is absorbed by the medium (before combustion) is sharply tilted. A transport medium can be described as a storage medium in that it is prevented from flowing out of the fuel region, such as whether it has been rolled over or rolled over.

Additionally or alternatively, the transport medium 410 was configured in a core, such as capillary action, from the bottom of the fuel chamber to the top of the transport medium 410, as more clearly shown in FIG. , Fibers, tubes, or other structures 424. In some embodiments, the plurality of glass fibers can be arranged to provide capillary action to move liquid fuel to the top of the transport medium 410. However, this is only one of many suitable structures for the medium 410 within the scope of this disclosure. Similarly, when glass or other absorbent and / or wicking and / or capillary fibers, strands or other structures 424 are used, they are arranged, woven and / or random. It can extend in any suitable orientation, including any configuration. The illustrated, non-limiting example in a non-woven configuration is a felt formed from fibers or strands. Additional examples include wool, blanket, mat, pad and sheet-shaped transport media. An example of a transport medium that has been found to be effective is Koaool ^™ , Cerablanket ^™ refractory ceramic fibers. However, other things can be used. The transport medium 410 may be referred to as a transport structure, and in some embodiments may be referred to as a storage structure.

  The transport medium 410 is not required for all embodiments, but may provide a flame holding surface for the fuel chamber. For example, the transport medium 410 may be coupled to the fuel processor 12, the hydrogen generation region 19, the fuel processor 12, the hydrogen generation region 19, by a predetermined distance to obtain desired thermal properties and heat transfer between the flame of the heating assembly 60 and the remaining components of the fuel processing assembly 10. It may be configured to provide a top surface for flame holding, or flame positioning, spaced from the evaporation zone 69 or other portions of the hydrogen generation assembly 10 and / or the fuel processing assembly 31. One advantage of utilizing the transport medium 410 is that the combustion flame is maintained at a consistent distance from other components throughout the combustion process, even when liquid fuel is consumed.

  The top 412 of the transport medium 410 is a first distance from the heating and ignition source 378, a second distance from the top member 404, a third distance from the evaporation region 69, and a fourth distance from the hydrogen generation region 19. And can be arranged at intervals. Any or all distances or any other spacing between the transport medium 410 and other members of the hydrogen generation assembly 10 may be varied to obtain a selected or desired heat transfer between the members. That is within the scope of the present disclosure. The first distance may be zero, or substantially zero, or the heating and ignition source may extend at least partially into the top surface of the transport medium, or the negative first distance It is within the scope of the present disclosure to extend below the top surface, which can be described as corresponding to.

  An example of a distribution conduit that can extend into the fuel chamber to deliver a liquid fuel flow into the fuel chamber is shown in FIG. When the fuel chamber includes a transport medium 410, the medium may be formed in the distribution conduit or otherwise extend around and / or be located on the distribution conduit. Can be included.

  It is within the scope of the present disclosure for the main burner assembly to extend into the liquid fuel region of the activation burner assembly. This structure is not essential, but this allows the flame to be generated with a burner assembly extending at the same or similar height. As will be described, the relative distance between the portion of the fuel processing assembly to be heated and the components of the heating assembly may vary within the scope of the present disclosure. In some embodiments, it may be preferable to keep these members relatively close together so that the heating value of the heated combustion stream is not reduced or otherwise inefficiently utilized. However, the shape and structure of the fuel processing assembly can provide structural limitations (ie space and size) that limit this arbitrary design object. The thickness of the burner assembly by forming a recess in the main burner assembly in the fuel region of the start burner assembly (e.g., instead of positioning the main burner assembly relative to the liquid fuel region of the start burner assembly), or Perhaps more specifically, the distance between the flame produced by the startup and main burner assembly and the hydrogen production region may be relatively reduced.

  When the fuel chamber includes a transport medium and a main burner assembly that extends into the liquid fuel region of the fuel chamber, the medium and burner assembly may be oriented in any suitable configuration in this region of the fuel chamber. By way of example and not limitation, the transport medium may extend on the opposite side of the main burner assembly and optionally below it, the main burner assembly being a recess in the transport medium. Or it can be accepted in other passages or the like.

  Another example of a hydrogen generation assembly 10 having a fuel processing assembly 31 having a heating assembly 60 according to the present disclosure is shown in FIGS. Although not specifically described, an exemplary fuel processing assembly may include any of the members, secondary members, and / or variations described, illustrated, and / or incorporated herein. Similarly, the elements and / or configurations newly described in FIGS. 18 and 19 are utilized in any of the other hydrogen generation and fuel processing assemblies described and illustrated and / or incorporated herein. Can be done. FIGS. 18 and 19 provide an example of a heating assembly 60 in which a main burner assembly 358 is disposed above the fuel chamber 376, including an activation burner assembly 356. The exemplary main burner assembly further includes a distribution conduit 67 that includes a transport medium 410 in the liquid fuel region 396 of the fuel chamber and is configured to transport a liquid fuel stream into the fuel chamber. Although not required, the exemplary conduit extends at least a substantial portion of the fuel chamber and is disposed along the conduit to open liquid fuel along the liquid fuel region. Can be included. 18 and 19 also provide a schematic example of a thermal ignition source 378 that includes a resistive element 400 positioned above the central region of the fuel chamber.

  In the illustrated example, the main burner assembly 358 is at least schematically illustrated with a main burner assembly that includes an opening 428 through which gaseous fuel flow from the main burner assembly is released and burned, along with the hydrogen generation and evaporation regions of the fuel processor. Including an elongate conduit extending in parallel. In the illustrated example, the main burner assembly 358 is configured to receive a byproduct stream 28 from a region 25 that includes a hydrogen generation region 19 and at least one purification region 24. Although not required, the illustrated region 25 includes a housing 27 that includes a hydrogen generation region 19 that may include a flow or other reforming catalyst. The housing 27 further includes at least one hydrogen selective membrane and / or methane production catalyst configured to separate the mixed gas stream produced in the hydrogen production region to the product hydrogen stream 14 and the byproduct stream 28. sell. FIG. 18 shows that the conduit through which the byproduct stream 28 flows before being consumed as gaseous fuel for the main burner assembly 358 provides back pressure to the system, thereby allowing more of the hydrogen gas to flow into the product hydrogen stream. It is also schematically illustrated that at least one filter 230 and / or at least one restrictive orifice 232 that facilitates a number of separations can be included, although not essential.

  FIGS. 18 and 19 also show that the fluid conduit forming the evaporation region 69 can include one or more pre-heating conduits 421 that are heated before the liquid feed stream evaporates in the evaporation region. . The preheating of the liquid feed stream is to evaporate the length of the evaporation zone and / or the time during which the feed stream evaporates in the evaporation zone and / or the liquid feed stream transported into the evaporation zone. The amount of heat generated, can be reduced. Preheating the liquid feed stream can also provide stability or stationarity of this stream. This is because if this stream evaporates rapidly, some liquid streams can cause a rapid (surging) flow.

  During the start-up of the hydrogen generation assembly (not all), having a feed transport system or other mechanism for utilizing the liquid combustible fuel flow for the heating assembly during start-up of the hydrogen generation assembly At least a portion is transported to the heating assembly as a liquid fuel stream. The liquid fuel stream is then ignited and combusted by the air stream or ambient air and produces a heated combustion stream that is used to heat the steam reformer. As described, in some embodiments, the fuel stream can have at least one of the same components as the hydrogen generating fluid, and in some embodiments, includes at least 25% water by volume. It may have the same composition as this stream, including but not limited to a composition.

  In some embodiments, a pump (eg, a positive displacement vacuum pump) can be used and configured to provide a predetermined volume of liquid fuel flow. This volume can also be described as a predetermined amount of liquid carbon-containing feedstock to the fuel chamber of the heating assembly. In some embodiments, the controller can be used to control the operation of the pump. In other embodiments, the pump can be operated manually and / or the predetermined volume can be manually injected or otherwise introduced into the fuel chamber. As described, the liquid fuel stream is transported to the fuel chamber and held therein as a liquid supply of fuel that is consumed at least during startup of the fuel processing assembly. Thus, unlike a heating assembly that is transported against it and consumes the fuel stream as is, the disclosed activation burner assembly temporarily stores at least the volume of liquid fuel. In some embodiments, the fuel stream may be configured to provide a carbon-containing feed stream at least during the start-up state and optionally during the (hydrogen production) operating state of the fuel processor.

  The fuel stream is transported to the fuel chamber and heated by a heated ignition source to increase the vapor pressure of the carbon-containing fuel in the fuel vapor region in the startup burner assembly. The fuel vapor is ignited by a heated ignition source and fuel combustion begins. Combustion heat adjacent to the ignition source can be radiated to heat adjacent liquid fuel, further increasing the vapor pressure of the carbon-containing fuel in the fuel chamber, and flame and combustion can propagate throughout the fuel chamber. . As described above, the temperature at which the fuel vapor ignites is determined by many factors. The fuel vapor is ignitable when the temperature of the fuel chamber adjacent to the heat ignition source reaches the ignition temperature. In some embodiments, the fuel vapor ignites immediately or is ignited when heated to the ignition temperature. In other embodiments, the fuel vapor is only when the surface temperature of the heating and ignition source reaches a heating element ignition temperature or a temperature that is hot enough for the surface of the heating element to ignite the fuel vapor (eg, incandescent or red hot). Ignite.

  The heating and ignition source may be significantly smaller than the size of the fuel chamber because combustion can propagate through the fuel chamber. For example, the heating and ignition source may be a localized heating source. The localized heating source is a heating element that is substantially smaller than the fuel chamber. The liquid fuel disposed in the fuel chamber has a top surface having a surface area. The localized heating source may be wound and linear, or otherwise configured as described above, and above or partially above the top surface of the liquid fuel. Can be arranged. The localized heating source may have a footprint (ie, occupied space) corresponding to the surface of the liquid fuel that corresponds to or is aligned with the heating source. The footprint of the localized heating source may be substantially smaller than the liquid fuel surface area of the fuel chamber. For example, the footprint may correspond to only 20% of the surface area of the liquid fuel region. In other embodiments, the thermal ignition source may be dimensioned to have a footprint that corresponds to only 10%, 5%, or less of the surface area. It is within the scope of the present disclosure that the heating and ignition source is greater than or corresponds to a greater percentage of the liquid fuel surface area, or that the heating and ignition source may be even smaller. The size of the heating and ignition source and the configuration of the fuel chamber (ie, baffle, presence of top member, placement of heating and ignition source, etc.) can affect the ignition temperature of the carbon-containing fuel, and also the heating element ignition temperature. May have an impact. Furthermore, as described above, the size and position of the ignition region and the combustion region are determined by the configuration of the heating ignition source.

  Once combustion is initiated in the startup burner assembly, combustion is continued, possibly supported by the transport medium, until the reformer or other hydrogen production zone is at least selected or at a predetermined temperature. . In an embodiment using a metering pump to transport a predetermined amount of carbon-containing feedstock into the fuel chamber, the amount of fuel transported is sufficient to raise the temperature of the hydrogen production region to a predetermined temperature. It can be calculated to include at least a carbon-containing feedstock. In some embodiments, the predetermined temperature at which the startup burner assembly is configured to heat the reformer is above or below the operating temperature of the hydrogen production region. For example, the starter burner assembly selected or predetermined temperature for raising the reformer exceeds a desired operating or reforming temperature by a predetermined amount, such as 25-125 ° C, 25-75 ° C, 50-100 ° C. Or less.

  In embodiments utilizing a metering pump that transports a predetermined amount of fuel to the activation burner assembly, the activation burner assembly can be configured to burn the fuel until all the fuel is burned. During this combustion, the main burner assembly can be activated to maintain the operating temperature of the fuel processing assembly. In the exothermic fuel processing assembly, the startup burner assembly may raise the fuel processing assembly to a predetermined temperature sufficient to begin operating the hydrogen generation mechanism and / or one or more feed streams for the fuel processor. Can be operated to evaporate or otherwise preheat. At this point, the exothermic reaction of the hydrogen generation region can be used to maintain the operating temperature of the hydrogen generation region.

  In embodiments that do not use a metering pump (or other transport mechanism configured to transport a predetermined amount of a fuel stream containing carbon to the fuel chamber), the hydrogen production region is heated to a predetermined temperature. Until then, the liquid combustible fuel stream can be transported to the activation burner assembly. In this embodiment, the predetermined temperature may still be lower than the temperatures described above (ie, there may be a greater difference between the predetermined temperature and the reforming temperature). One reason for this is that when the flow of fuel flow to the start burner assembly stops, the fuel chamber may contain a quantity of liquid fuel that is not yet combusted. This liquid fuel is combusted to further raise the temperature of the hydrogen generation assembly, even with the anode where the flow of the liquid combustible fuel stream has stopped flowing to the starting burner assembly.

  Compared to embodiments having a metering pump, embodiments having a continuous flow of fuel to the starter burner assembly are at least one additional, such as a temperature or time based flow controller and / or liquid fuel, ignition chamber separator May have special characteristics. A temperature or time-based flow controller can either enter the activation burner assembly when a predetermined temperature is reached, either by measuring the temperature directly or by measuring time and comparing this to an empirical temperature / time table. The liquid combustible fuel flow may be configured to stop suddenly or gradually automatically. It is within the scope of the present disclosure that the flow of the fuel stream can be manually controlled in some embodiments. In addition, the activation burner assembly may include a liquid fuel ignition chamber separator to prevent newly added fuel and carbon-containing feedstock from cooling liquid fuel that has already been heated by the heated ignition source.

  The start-up heating assembly also utilizes a metering pump to provide an initial amount of liquid fuel to heat and ignite to ensure continued combustion until a predetermined temperature is achieved. It is within the scope of the present disclosure that a continuous supply of liquid combustible fuel stream is subsequently initiated.

  Regardless of whether a metering pump and a predetermined volume are utilized, the fuel stream is continuously fed or heated under a heating of the hydrogen generation area to a predetermined temperature at which the feed stream can be transported to the hydrogen generation area. Several combinations of the two can be used, the feed stream can be introduced into the reforming zone, and hydrogen production can be initiated. In embodiments where a common stream is used as a feed stream and a fuel stream, such as a composite stream containing water and a carbon-containing feedstock, the transition between supplying a fuel stream and supplying a feed stream. May be instantaneous, stepped, or provide a fuel stream and there may be a break between supplying a feed stream that is used to deliver a predetermined amount of fuel to a heating assembly by a metering pump. There may be.

  As hydrogen gas is generated in the reforming region of the steam reformer and subsequently purified in one or more purification regions, a by-product stream of gas is generated and delivered to the heating assembly, the main burner assembly Can be used as a fuel flow. In some applications, such as many steam reformers where the carbon-containing feedstock is methanol, the by-product stream is optional (eg, an additional carbon-containing feedstock from the feed stream for the hydrogen production zone). The additional liquid fuel must also have sufficient heating value that the heating assembly does not require. However, when other carbon-containing feedstocks and especially hydrocarbons are used, continue to feed carbon-containing feedstocks (such as feedstreams or other sources) to the main burner assembly and / or reforming It may be necessary to use several product hydrogen streams as the fuel stream to provide sufficient fuel to maintain the temperature of the device.

  FIGS. 20-22 illustrate a non-illustrated housing of a fuel processing assembly 31 having a heating assembly 60 configured to receive a liquid combustible fuel stream to assist in at least activation of the fuel processing assembly. A limited embodiment is shown. As shown, the assembly includes an outer shell 68 and various optional outer heat shields and supports. The illustrated example includes an activation burner assembly that is configured to receive a liquid fuel stream that combusts to heat at least a hydrogen generation region of the fuel processing assembly to a temperature that produces suitable hydrogen. The liquid fuel stream includes at least one combustible liquid fuel (eg, methanol). This liquid fuel is not essential, but contains water (eg, at least 25% by volume of water) and can have the same configuration as the feed stream in which hydrogen gas occurs in the hydrogen production zone (but not necessarily). Absent). An additional example of a suitable liquid activation burner (and variations thereof and optional components therefor) is the name “Hydrogen-Producing Fuel Processing Assemblies, Heating Assemblies, and Methods of Filing, filed on September 13, 2005. Operating the Same ", U.S. Patent Application No. 11 / 226,810, the entire disclosure of which is hereby incorporated by reference in its entirety for all purposes. At least in the lower right portion of FIG. 21, an optional restriction orifice 232 and filter 230 are heated that can be used to heat at least the hydrogen generation region of the fuel processing assembly during the hydrogen generation operation of the fuel processing assembly. A fluid conduit defining a flow path for the by-product stream from a separation region (eg, a membrane-based separation region) having the illustrated by-product stream transported to a burner that combusts the by-product stream to produce a combustion stream Indicated by The example hydrogen generation assembly 10 shown in FIGS. 20-22 is described, illustrated and / or incorporated herein in a liquid receiving heating assembly, fuel and / or feed stream composition, fuel processing assembly. , Purification region, etc. In certain embodiments, the assembly 10 is shown to include the shell 27 of FIGS. 9-11 and the heating assembly of FIG.

  As noted above, the hydrogen generation assembly 10 according to the present disclosure may utilize any suitable type and / or number of feed transport systems 22 suitable for the feed and / or fuel stream being transported. As described, some feed transport systems include pumps or other electrically driven propulsion mechanisms. On the other hand, others do not require a pump or otherwise do not utilize a pump. Some feed transport systems are in fluid communication with a pressurized supply (112) of fuel or feed. On the other hand, others are in fluid communication with a non-pressurized or low-pressure supply that requires an external force to propel fluid to a fuel processing assembly, such as a hydrogen generation zone or its heating assembly. . It is also within the scope of the present disclosure that fuel and feed streams can be stored and transported separately, but this complete separation is not necessary, as shown in FIGS. It is within the scope of the present disclosure that exemplary feed transport systems can be selectively utilized from any of the permissible hydrogen generation assemblies described, illustrated and / or incorporated herein. Is within.

  According to one aspect of the present disclosure, although not required for all embodiments, the liquid phase carbon-containing feedstock 84 is formed in the reformed region 19 as illustrated schematically in FIG. Can be used for feed portion 18 containing carbon in feed stream 16 and feed portion 65 containing carbon in fuel stream 64 for heating assembly 60. This dual use of carbon-containing feedstock 84 is not necessary for all embodiments of the present disclosure. FIG. 23 illustrates a plurality of feed transport systems 22 (eg, a transport system 22 configured to transport water 17 containing a feed stream, a feed stream containing a carbon-containing feedstock 18, and / or A graphical representation of a hydrogen generating fuel processing assembly including a feedstock transport system 22) configured to transport a fuel stream 64 is also provided. As illustrated by the dashed line in FIG. 23, the foregoing example of three feed transport systems is a single feed (which may include multiple pumps and / or generate multiple outlet streams). It is within the scope of the present disclosure that additional or alternative implementations for the material transport system 22 may be implemented. It is further within the scope of the present disclosure that not all liquid streams to the fuel processing assembly are transported by the feed transport system 22. Instead, one or more streams can be transported by different mechanisms or transport systems.

  In the example shown in FIG. 23, the liquid carbon-containing feedstock 84 is transported to the heating assembly 60 and the hydrogen generation zone 19. Since the fuel processor 12 can have various configurations such as a configuration not including the purification region, a configuration having a plurality of types and numbers of purification mechanisms, and the like, FIG. 23 is shown in a fragmentary view. The fragmentary fuel processor schematically shown in FIG. 23 (and the following figures) is described in this specification, illustrated and / or with any of the steam reformers and other fuel processors incorporated. Likewise, it is intended to schematically represent any of these configurations.

  FIG. 24 is similar to FIG. 23 except for the following points. That is, the liquid carbon-containing feedstock 84 is transported as a single stream to the valve assembly 86, in which the carbon-containing feedstock is selectively transported to at least one of the heating assembly and the hydrogen generation zone. The valve assembly 86 can include any suitable structure for selectively separating the carbon-containing feed stream at the heating assembly and the hydrogen production zone. A range of possible configurations includes a heating assembly that receives all of the carbon-containing feedstock and a hydrogen generation zone that receives all of the carbon-containing feedstock, or a heating assembly and hydrogen generation zone that receives the carbon-containing feedstock. It is. As described herein, the distribution of the carbon-containing feedstock is dependent on the particular carbon-containing feedstock used, whether the byproduct stream 28 is used as a fuel for at least some heating assemblies 60, And the particular operating mode of the fuel processor (eg, idle mode, start-up mode or hydrogen production mode).

  The distribution of the liquid carbon-containing feedstock 84 between the hydrogen generation zone and the heating assembly can be controlled manually. However, in many embodiments, the distribution is predetermined and / or at least partially automated, for example, by including a controller 88 that selectively controls the transport of feedstock 84 between the hydrogen generation zone and the heating assembly. It can be preferred. An example of a suitable controller for a steam reforming fuel processor is disclosed in US Pat. No. 6,383,670, the complete disclosure of which is incorporated herein by reference. In some embodiments, controller 88 and / or valve assembly 86 may be configured to allow a predetermined initial volume of carbon-containing feed to heating assembly 60. This is then described in more detail herein.

  As noted above, with respect to a steam reformer or other fuel processor that produces hydrogen from water and a carbon-containing feedstock, the feedstream 16 is at least substantially and typically completely submerged in water or water. And preferably a miscible liquid phase carbon-containing feedstock 84 and a mixture of water. Thus, a single (composite) feed stream 90 containing water 17 and carbon-containing feedstock 84, similar to heated assembly fuel stream 64, is a hydrogen production feed stream 16 for the reforming reaction. Can be consumed as Further reductions in feeds, transport systems, flow control valves, transport conduits, etc., include feed streams that include the same liquid carbon-containing feedstock 84 and water 17, including carbon-containing feedstocks that can preferably be mixed into water. 16 and fuel stream 64 may be achieved in another aspect of the present disclosure. This is illustrated schematically in FIGS. 25 and 26 and this combined flow is shown at 90. These streams 16 and 64 can have almost or completely the same composition and can be formed entirely from stream 90. However, at least one stream 16 and 64 may have at least one additional component or amount of water or carbon-containing feedstock that is increased relative to the stream before it is consumed by the heating assembly or hydrogen production zone. Is within the scope of the disclosure. Similarly, it is within the scope of the present disclosure that additional streams can transport additional components or amounts of water or carbon-containing feedstock to a heating assembly or fuel processor.

  (Only the carbon-containing feedstock component 84 of the feedstream 16 is transported to the heating assembly 60 rather than the carbon-containing feedstock 84 and the water 17) Similar to the previous alternative of FIGS. 23 and 24, FIG. As illustrated schematically in FIG. 1, the composite feed stream 90 can be selectively transported to the heating assembly 60 and the hydrogen generation zone 19 in separate streams from the same or different sources. Alternatively, and as shown schematically in FIG. 26, a single composite feed stream 90 may be transported to the fuel processing assembly, and more particularly to the valve assembly 86. Here, this flow is selectively divided in the heating assembly and the hydrogen production zone. The controller 88 may be a manual controller or a computerized or other electronic control device or a program-controlled controller and is also shown in the dashed line in FIG. The controller 88 may be located in the internal or external fuel processor 12 and / or may include internal and external members.

  The relative amounts of water 17 and liquid carbon-containing feedstock 84 in the composite feedstream 90 can vary within the scope of the present disclosure. For example, this ratio can be derived from the specific carbon-containing feedstock used, the hydrogen generation mechanism used in the fuel processor, user preferences, the catalyst used, the demand for hydrogen gas, the efficiency of the reforming catalyst, etc. It can depend on factors such as And the relative concentrations of these components can be expressed in relation to the ratio of water to carbon. When the feedstock 84 is methanol, it has been shown to be effective that the molecular ratio of vapor to carbon is 1: 1. When the feedstock 84 is ethanol, it has been shown to be effective that the molecular ratio of vapor to carbon is 2-3: 1. When the feedstock 84 is a hydrocarbon, an approximately 3: 1 vapor to carbon ratio is typically used. However, the above illustrated ratios are not meant to be exclusive ratios within the scope of the disclosure, and others including larger and smaller ratios may be used.

  In FIG. 27, a variation of the configuration of FIG. 26 indicates that it is within the scope of the present disclosure that the valve assembly 86 may be located inside or outside the fuel processor assembly 31. FIG. 27 shows that the gas byproduct stream 28 is used as a gaseous fuel for the heating assembly when the fuel processor includes a purification zone 24 that produces a gas byproduct stream 28 or otherwise associated. It also shows that it can be transported to a heating assembly. This gaseous fuel may be supplemented with the liquid fuel described above (eg, carbon-containing feedstock 84 or composite feedstream 90), or a specific steam reformer or other fuel processor and / or a specific fuel processor. It may contain a sufficient calorific value for the configuration of operation.

  Another exemplary, non-limiting example suitable feed transport system 22 that may be used with the hydrogen generation assembly 10 according to the present disclosure is shown in FIG. 28 and the hydrogen of the fuel processor 12 of the fuel processing assembly 31. A feed stream 16 is configured to be transported to the production zone 19. As shown, the feed transport system 22 includes a pump assembly 100 that includes at least one pump 102. The pump 102 includes an inlet 106 and an outlet 108. The inlet is in fluid communication with a feedstock supply or source 112, and the outlet is in fluid communication with the fuel processor 12. Pump 102 further includes an actuating portion or pumping mechanism 109 that is normally located between the inlet and outlet of the pump. Pump 102 is configured to draw or otherwise receive liquid stream 110 from supply 112 and discharge liquid stream 116. Accordingly, the feed transport system 22 can be described as being configured to pump a liquid stream containing at least one feed for the hydrogen production region 19 from the liquid feed supply. Liquid stream 110 may be referred to as an inlet stream or suction stream, and liquid stream 116 may be referred to as an outlet stream.

  The pump 102 can be driven by any suitable power supply. This illustrative non-limiting example includes components of the hydrogen generating fuel cell system 42, such as the fuel cell stack 40 and / or energy storage 52. An additional example includes a power supply that is independent of the output generated by the fuel cell system, such as an external or dedicated battery, a distribution network, or the like. Although not required, the pump 102 is configured in an on or driven form in which the pump accepts the liquid stream 110 and discharges the liquid stream 116, or is configured in an off or non-driven form in which the pump does not discharge the liquid stream 116. It may be a single speed or single output pump. The actual output of the pump depends on the voltage of the drive output supplied to the pump, which tends to change.

  As described, pump assembly 100 includes at least one pump. Accordingly, it is within the scope of the present disclosure that the pump assembly 100 can include a single pump 102 or multiple pumps 102. When the pump assembly includes multiple pumps, these pumps can cooperate to draw liquid stream 110 and / or discharge outlet stream 116. Additionally or alternatively, these pumps can each be configured to draw liquid stream 110 from and / or discharge outlet stream 116 from the same or different sources 112.

  The supply 112 includes any suitable type and / or number of reservoirs and / or other sources from which liquid flow can be drawn or received by the inlet 106 of the pump 102 of the pump assembly 100. Suitable supplies 112 in the illustrated non-limiting example include pressurized or non-pressurized tanks, small cans, and other liquid containers. The liquid stream 110 includes at least one component of the feed stream 16 (eg, water 17 and / or carbon-containing feedstock 18). As indicated by the dashed line in FIG. 28 and as described herein, the liquid stream 110 and / or the feed 112 may contain at least two different components of the feed stream 16 (eg, water 17 and liquid carbon containing). It is within the scope of the present disclosure to include feedstock 18). Accordingly, the liquid stream 110 may include a single component of the feed stream 16, may include multiple components of the feed stream 16, and / or may include all of the component or components of the feed stream 16. It may be included within the scope of the present disclosure. The component or components of the feed stream 16 may be referred to as a feedstock in which the hydrogen production region 19 produces hydrogen gas.

  As shown in FIG. 28, at least a portion of the liquid outlet stream 116 may form a feed stream 16. However, at least a portion of the liquid stream 116 may additionally or alternatively be located upstream of the pump inlet 106 (eg, to the supply 112 or a fluid conduit where the liquid stream 110 flows from the supply 112 to the pump 102). Can be reused. As used herein, the terms “upstream” and “downstream” are measured with respect to the direction of fluid flow through the corresponding flow. The recycled portion 120 of the liquid stream 116 is shown as a solid line that is being transported to the supply 112 and as a dashed line that is being transported to the fluid conduit containing the liquid stream 110. It is within the scope of the present disclosure that the recycle stream 120 can be recycled directly to the pump, such as at or near the inlet 106, as shown by the dashed line in FIG.

  As described schematically in FIG. 29, as described with respect to the fluid conduit of the feed transport system 22 or associated therewith, the feed transport system is a liquid that is drawn or received from the supply 112 to the pump 102. It can be described as including an intake conduit 130 through which the flow 110 passes. The feed transport system further includes an outlet or output conduit 132 through which the liquid stream 116 discharged from the pump outlet 108. The outlet conduit is in fluid communication with a transport conduit 134 that passes at least a portion of the liquid stream 116 that can be transported to the hydrogen production region 19 as at least a portion of the feed stream 16. The feed transport system 22 according to the present disclosure further includes a recycle conduit 136 that defines a fluid flow path that establishes fluid communication between a portion of the feed transport system upstream of the working portion of the pump and the transport conduit. This portion of the recycle conduit may be referred to as the higher pressure region of the recycle conduit, and the portion of the recycle conduit downstream of the flow restrictor may be referred to as the lower pressure region of the recycle conduit. Represented in slightly different terms, the recycle conduit extends in fluid communication between the outlet conduit and the flow restrictor and defines a flow path therebetween, and the flow restrictor; It may be described as including a feed portion 112, an inlet conduit 130, or other portion of the feed transport system upstream from the working portion of the pump, and a second portion extending in fluid communication. The second portion of the recycle conduit similarly defines a liquid flow path between the flow restrictor and this upstream portion of the feed transport system.

  In the example shown in FIG. 29, the outlet conduit branches to establish recycling and fluid communication or connection with the outlet conduit. The fluid conduits described herein can include any suitable structure that defines a flow path for the liquid or other fluid flow described herein. Accordingly, the conduit must be formed of the appropriate material, structure and size for the operating conditions through which the fluid flow is encountered and thereby. Such a conduit is schematically illustrated in FIG. 29 and may include or communicate with additional structures and / or members such as sensors, valves, flow regulators, etc. Within range.

  While not required in all embodiments, it is within the scope of the present disclosure for pump 102 to be configured to continuously draw liquid stream 110 and discharge liquid stream 116 therefrom. The pump is transported at a higher flow rate of the feed stream 116 than desired, or in some embodiments, a higher flow rate of the feed stream 116 than may be present in the feed stream 116. It is also within the scope of the present disclosure to be configured as such. Accordingly, the pump can be described as providing an output stream having a liquid flow rate that is greater than the flow rate of the feed stream 16 that is transported to the hydrogen generation region (or other portion) of the fuel processor 12 and produced. In this type of configuration, it can be described that the pump can be configured to provide excess liquid or excess flow rate in the output stream 116, thereby providing a flow of liquid that forms a recycle stream 136. .

  By maintaining the pump in an operating condition that provides an output stream 116 that includes a greater amount of feedstock than is required by the hydrogen production zone, the pump is capable of generating hydrogen when the hydrogen production zone is at least in the hydrogen production operating state. It can be configured to maintain a constant output regardless of demand or demand of the hydrogen production region. In some embodiments, the pump may provide a maximum demand for a hydrogen production area for the feedstock (ie, when the hydrogen production area is at its maximum rated production rate and / or It can be configured to maintain a liquid feed flow rate that exceeds the feedstock requirement) when producing sufficient hydrogen gas to provide power at the maximum rated drive output. In some embodiments, the feed transport system provides an output stream having a flow rate that is at least 10%, at least 25%, or at least 50% greater than the amount of feed required by the hydrogen production zone. Can be configured. However, due to the automatic control characteristics of the feed transport system, surplus feed is not wasted, but instead is recycled (recycled) to the feed transport system where it is reused or supplied to the feed. Can be returned.

  28 and 29, the feed transport system 22 further includes a flow restrictor 140 and a pressure actuated valve 150. The flow restrictor 140 is configured to reduce or limit the cross-sectional area of the recycle conduit 136. For example, as shown schematically in FIG. 29, the flow restrictor 140 may define a cross-sectional area for the conduit 134 that is smaller than the cross-sectional area of the transport conduit. Accordingly, the liquid stream 116 can be biased to flow through the transport conduit 134 and thereby to the flow to the hydrogen production region 19. At this time, the pressure of the hydrogen generation region and / or the transport conduit 134 is less than the pressure of the recycle stream (at least between the outlet conduit 132 and the flow restrictor 140). As represented in slightly different terms, the flow restrictor 140 is a recycle that flows through the flow restrictor back to the feedstock supply or other upstream portion of the working portion of the pump and through the recycle conduit 136. A back pressure for the flow 120 is configured to be generated. The amount of back pressure selected by the orifice depends on various factors (eg, one or more user preferences, orifice size, orifice shape, flow rate of liquid produced by the pump assembly, transport and recycling conduits Size, feed stream composition and properties, etc.). Preferably, the flow restrictor is greater than the selected or desired transport pressure of the feed stream 16 to the hydrogen production zone 19 and less than the threshold transport pressure and / or threshold recycle pressure described below. Sized or otherwise configured to provide or maintain pressure.

  The flow restrictor 140 may include any suitable structure configured to limit the flow path of the recycle stream by the recycle conduit 136. By way of example and not limitation, the flow restrictor includes an orifice 142 having a cross-sectional opening 144 that is smaller than some recycle conduits 136 upstream of the orifice 142 and / or smaller than the transport conduit 134. May be included. An example of this type of orifice is illustrated schematically in FIG. Orifice 142 may be referred to as a limiting orifice. The orifice 142 may have an opening of a constant or non-adjustable size. Alternatively, the flow restrictor may include an orifice having a variable or adjustable opening size. When the orifice is configured to allow adjustment of its orifice size, the orifice may be configured to manually adjust the orifice size, such as in response to user input to a manual control element, and Alternatively, the fuel processing assembly and / or the fuel cell system may be configured to respond to electrical or other control signals from a controller or other portion.

  The pressure actuated valve 150 avoids the back pressure generated by the restriction orifice 142 or other flow restrictor 140 by which the recycle flow bypasses the flow restrictor, but upstream of the working portion of the pump. It is configured to selectively allow return to the feed or other part of a feed transport system. A suitable pressure-actuated valve in the non-limiting example shown is fluidly connected as described herein, i.e. to a bypass conduit that allows liquid to bypass the flow restrictor. Includes pressure safety valves and check valves to selectively restrict or allow liquid flow. As visually shown in FIG. 29, the pressure actuated valve 150 can selectively flow at least a portion of the recycle stream 136 as a bypass stream 154 from an upstream position of the flow restrictor to a downstream position of the flow restrictor. In fluid communication with the bypass conduit 152. As expressed in more structural terms, a pressure-actuated valve is not fed through a flow restrictor, but at least a portion of the recycle stream from the conduit 130 is routed through the recycle conduit to the supply 112 or inlet conduit 110. It is configured to selectively allow the flow to the In FIG. 28, the pressure activated valve is schematically illustrated with a connection between the bypass conduit and the recycle conduit upstream of the flow restrictor. However, the pressure-actuated valve is in any suitable location where the flow to the flow restrictor can be restricted and allowed, along with the flow that can be transported through the bypass conduit when the pressure-actuated valve restricts the flow to the flow restrictor. It is within the scope of the present disclosure to be located. For example, FIG. 29 shows that a pressure-actuated valve can be located at an intermediate point along the bypass conduit (ie, anywhere between the inlet and outlet of the bypass conduit). It is also within the scope of the present disclosure that the valve may be located at the inlet or outlet of the conduit.

  The pressure activated valve 150 causes flow through the bypass conduit 152 when the pressure in the recycle stream 136 upstream of the flow restrictor (ie, between the output line 132 and the flow restrictor 140) is less than the threshold recycle pressure. Usually configured or biased to limit. This configuration may be referred to as a pressure-actuated valve closed setting or flow restriction configuration. However, when the pressure reaches (or exceeds) this threshold recycle pressure, the pressure-actuated valve is configured to automatically allow liquid from upstream of the orifice 140 to flow through the bypass conduit 152.

  When the pressure reaches (or exceeds) this threshold recycle pressure, and at least a portion of the recycle stream 120 is bypassed when the pressure activated valve is configured to respond (automatically) to its operational setting. Flowing through, thereby reducing the pressure of the liquid upstream of the flow restrictor. This can also reduce the pressure of the feed stream transported by the feed transport system. This threshold recycle pressure may be the same as the maximum or threshold transport pressure acceptable for the feed stream 16. However, it is also within the scope of the present disclosure that these pressures are not the same. For example, the threshold recycle pressure may be a pressure set so that the pressure-actuated valve allows flow through the bypass conduit (and thereby reduce transport and other related flow pressures), the transport conduit and / or Or, the fuel processing assembly can be selected below a threshold transport pressure, such as by a determined increase, to provide a buffer or pressure differential with a maximum pressure set or desired to receive the feed stream.

  As shown herein, at least the hydrogen production region of the fuel processing assembly 31 may be designed to operate at a high pressure, such as at least 50 psi. When the fuel processing assembly includes a purification or separation region, for example as described herein, this region may also be designed to operate at high pressure. The specific maximum and minimum operating pressures for a particular fuel processing assembly tend to vary based on various possible factors. An example of this type of factor is the hydrogen production reaction utilized in the hydrogen production zone 19, the composition of the feed stream 16, the viscosity of the liquid in the feed stream 16, the structure, dimensions, and / or placement of the transport conduit. May include, but is not limited to, the configuration of the combustion processing assembly, the pressure requirements of the fuel processing assembly, and / or downstream of the fuel cell system from the hydrogen generation region, design choices, tolerances, and the like. For example, some fuel processing assemblies are preferably maintained at a high pressure downstream of the hydrogen production zone and optionally in at least one hydrogen production zone, and optionally in at least one purification zone. By using a restriction orifice or other suitable flow restrictor downstream of the clean zone, it can be designed to maintain high pressure.

  The amount of liquid flowing through conduit 152 (ie, the percentage of recycle stream 120) can vary within the scope of the present disclosure. In some embodiments, the entire flow forming the recycle stream 120 may flow through a bypass conduit when the pressure activated valve is in operation or configured to allow flow. In other embodiments, some recycle streams 120 may flow through the orifice 142 or other flow restrictor 140 even while the pressure activated valve is at this operational setting.

  When a pressure-actuated valve 150 is present, the actuated valve 150 includes a valve, or member 156 thereof, and a biasing mechanism 158 configured to bias the valve to a position closer to its operating setting. May be included. The biasing mechanism 150 provides any biasing force as described above when the circulating pressure threshold is reached or exceeded, and is any suitable configuration configured to allow the pressure-actuated valve to be placed in its operational setting. May include structures or equipment. A suitable biasing mechanism in the illustrated non-limiting example is a spring that exerts a biasing force against the valve member in a direction opposite to the force acting on the pressure-actuated valve by the recycle stream liquid upstream of the flow restrictor. Or other elastic members. In other words, the liquid flow upstream from the flow restrictor can exert a force that presses the pressure actuated valve from its closed position to its operational setting. This force is applied to the bias by the biasing mechanism 158 or to the force exerted by the biasing mechanism 158. When the force generated by this flow exceeds the force operated by the biasing mechanism, the pressure-actuated valve is set to its operating setting. Otherwise, the pressure-actuated valve is configured to remain in its closed setting when the fluid pressure is exerted on the pressure-actuated valve with less force than that applied by the biasing mechanism. The biasing mechanism 158 is as a pressure detector or pressure sensor configured to detect when the pressure of the liquid stream discharged by the pump assembly exceeds a pressure threshold, such as a recycle pressure threshold or a transport pressure threshold. Can also work. Specifically, the threshold pressure is exceeded when the liquid pressure as applied to the biasing mechanism sufficiently exceeds the force operating by the biasing mechanism. Thus, the biasing mechanism can be configured to exert a biasing force that is fixed at or corresponding to a threshold pressure (eg, a recycling pressure threshold or a transport pressure threshold).

  When the pressure detected (or applied) decreases below the recycle pressure threshold, when the pressure decreases to a level that is not sufficient to overcome the biasing force exerted by the biasing mechanism, and / or The biasing mechanism 158 is preferably configured to automatically return the pressure activated valve to its closed setting when a predetermined time has elapsed since the pressure activated valve was set to its operational setting. In other words, it is within the scope of the present disclosure that once set, the pressure activated valve is configured to maintain its operational setting for at least a predetermined minimum period of time. It is also within the scope of the present disclosure that the pressure-actuated valve can be configured to automatically transition between an operational setting and a closed setting in full response to the force exerted by the liquid vapor and biasing mechanism. It is.

  28 and 29 illustrate a feed transport system 22 that includes a flow restrictor and a pressure-actuated valve associated with the recycle stream of the feed transport system. In operation, the orifice 142 or other flow restrictor 140 generates a back pressure that propels or biases the output flow from the pump assembly toward the hydrogen generation region of the fuel processing assembly via the transport conduit 134. It is configured. However, if the orifice or other flow restrictor becomes clogged or fails, the back pressure value generated by the flow restrictor increases and the portion of the liquid outlet stream 116 that flows to form the recycle stream 136 is increased. Decrease or even become zero. This corresponds to when there is no flow through the flow restrictor. If this pressure continues to increase, i.e., if the hydrogen generation assembly remains operational, damage or damage is possible. For example, pressures that exceed the transport pressure threshold and / or the recycle pressure threshold can damage the pump 102 or one or more portions of the fuel processing assembly. Because the pump 19 is configured to discharge a higher flow rate of the output stream 116 than is consumed in the hydrogen production zone 19, at least in the output stream 116, and typically in the feed stream 16, and The pressure in the portion of the recycle stream 120 from the flow restrictor continues to increase in nature. The pressure increases because the orifice or other flow restrictor cannot tolerate the surplus liquid or sufficient amount of surplus liquid flowing to form the recycle stream 120. However, since the feed transport system described above also includes a pressure activated valve 150, the pressure is prevented from increasing beyond the recycle pressure threshold or the transport pressure threshold. When the pressure actuated valve is activated, the pressure decreases until at least the pressure actuated valve return returns to the closed setting. If the flow restrictor is continuously clogged or otherwise not working or only partially working, the pressure will start to increase again and again by means of a pressure operated valve that is transitioning to its operating setting, The pressure increases again or exceeds the corresponding pressure threshold.

  It is within the scope of the present disclosure that the feed transport system 22 according to the present disclosure may not include the flow restrictor 140 and the pressure actuated valve 150. For example, the feed transport system may include a flow restrictor 140 as described herein without a pressure activated valve (and thus without a bypass conduit 152). As another example, a feed transport system may include a pressure-limiting valve 150 as described herein that selectively bypasses the pressure-actuated valve with a pressure-actuated valve that generates a back pressure for the outlet flow. Can be included without a vessel. In such an embodiment, there is no bypass conduit and the pressure-actuated valve selectively generates a back pressure in the outlet (and transport) stream in its closed setting, and the recycle stream flow Is limited by a pressure actuated valve. As described herein, when the pressure exceeds the pressure threshold, the pressure-actuated valve is transitioned or propelled to its operational setting, where at least a portion of the outlet flow is supplied to the supply 112 or Reused in other parts of the transport system upstream of the working part of the pump.

  As described, the system 22 does not include a pressure-actuated valve and the selected pressure threshold is exceeded when the flow restrictor fails, is clogged, or cannot function properly. Pressure may increase. However, the fuel cell system, including the system 22, and / or the fuel processing assembly, and / or the feed transport system 22, is for detecting and responding to pressures that are close to or exceeding the selected pressure threshold. Other suitable mechanisms may be included. For example, a system that includes a controller that is configured to control operation of the feed transport system 22 in response to a pressure that is at least close to or approaching a selected threshold may include an output stream 116 upstream of the flow restrictor 140. Or a pressure sensor configured to measure pressure at other suitable locations.

  As another example, if the feed transport system 22 is implemented without a flow restrictor, the pressure actuated valve 150 selects the output stream 116, the feed stream 16, and other pressures, and the pressures of these streams are selected. It is still possible to selectively reduce in response to exceeding a pressure threshold (such as the recycle pressure threshold or transport pressure threshold described above). Since such a feed transport system 22 does not include a flow restrictor that sets some back pressure within the system 22 but allows recycle flow, the system pressure tends to oscillate. More specifically, the liquid pressure tends to increase as the pump produces a higher liquid flow rate than is consumed in the hydrogen production region 19. This increase tends to continue until the pressure actuated valve transitions from the closed setting to the operating setting. Thereafter, the pressure tends to decrease until the pressure actuated valve returns to its closed setting, at which time the liquid pressure tends to begin increasing again. This oscillation of the liquid pressure, such as the pressure of the feed stream 16, can affect the flow rate of hydrogen gas produced by the fuel processor and can affect the output produced by the fuel cell stack. The system must still be active, but the operating state may not be maintained steady or constant due to pressure fluctuations or vibrations in the feed transport system.

  As described, some feed transport systems 22 according to the present disclosure are therefore configured to transport liquid and gas streams. A non-limiting example of such a feed transport system includes a liquid hydrogen production fluid (15) in the hydrogen production region of the fuel processing assembly and a gas combustible fuel stream (13) in the heating assembly. Or vice versa. FIGS. 31-35 provide illustrative, non-limiting examples of feed transport systems that are configured to selectively and individually transport liquid and gas streams.

  In one example, the feed transport system 22 includes a pressurized source 499 of heated fuel 13 and hydrogen generating fluid 15. An example of source 499 includes a pressurized tank or other pressure vessel that contains one or both of fuel 13 and fluid 15 under pressure. However, any suitable pressurized source can be used within the scope of this disclosure. Because these components of the feed stream 11 are available under pressure from the feed transport system, the hydrogen generation assembly 10 may receive heated fuel and / or hydrogen generation fluid from a mechanical pump, compressor, or source 499. It does not require the use of other electric drive members to draw and transport this stream under pressure to the hydrogen generation area of the fuel processing system 31 and the heating assembly. Instead, these flows are automatically generated from a pressurized source upon opening a valve or other suitable flow control device that selectively permits or restricts the flow from the feed transport system to the fuel processing system. Promoted. These flow restriction devices are schematically illustrated in FIG. 30 and are collectively referred to as a valve assembly 460. Exemplary delivery pressures for the hydrogen production region 19 are generally in the range of 50-300 psi. However, pressures outside this range are also within the scope of the present disclosure. Non-limiting examples of transport pressures are 100-250 psi, 125-225 psi, 150-225 psi, 175-225 psi, 150, as the contents of the hydrogen production region that utilizes a steam reforming catalyst to produce a mixed gas stream 20. -200 psi, at least 100 psi, at least 150 psi, at least 200 psi, and transport pressures of less than 250 psi and at least 100 or 150 psi.

  FIG. 31 provides an example of a feed transport system 22 that includes heated fuel 13 and hydrogen generating fluid 15 in a pressurized source 499 in the form of a separate pressure vessel 459. In such an embodiment, each of the fuel 13 and fluid 15 is a container 459 configured to transport a gas or pressurized liquid stored under pressure to a hydrogen generation region of the fuel processing system. It is a liquid stored in The illustrated example of a suitable mechanism for transporting a liquid stream at a suitable pressure from the feed transport system 22 without requiring the use of mechanical and / or electric pumps, compressors or similar equipment, It includes a gaseous propellant that pressurizes the liquid from the feed transport system and propels the liquid flow depending on the valve assembly 460 that is tolerated. An example of a suitable propellant includes carbon dioxide and nitrogen gas. However, other things can be used.

  The feed transport system 22 has a pressure vessel 459 containing heated fuel 13 and hydrogen generating fluid 15 and individually transports a stream containing fuel or fluid, such as in response to the configuration of the valve assembly. It is within the scope of this disclosure to include a configured pressure vessel 459. An example of this type of feed transport system is shown in FIG. The pressure vessel 459 is configured to store the heated fuel 13 and the hydrogen generating fluid 15.

  In the container 459, one of the fuel 13 and fluid 15 is configured to be released under its own pressure while the other of the fuel 13 and fluid 15 is composed of the fuel 13 and fluid 15. It can be configured to be released from the pressure vessel under an applied pressure, such as from a first one. For example, the heated fuel may be placed in a pressure vessel under its own pressure for transport to the heating assembly 460. The hydrogen generation fluid may be placed in a pressure vessel 459 for transport to the hydrogen generation region 19 under pressure applied by heated fuel. The hydrogen generating fluid and the heated fuel are kept substantially separate at least in the pressure vessel, such as the internal cavity of the pressure vessel. This means that the fuel 13 and the fluid 15 are not mixed throughout the pressure vessel. Instead, the heated fuel and hydrogen generating fluid are maintained in a region that is separately distinguishable in the pressure vessel with little or no mixing of fuel 13 and fluid 15. For example, the heated fuel may be a gas and the hydrogen generating fluid may be a liquid, and the fuel and fluid may be separated by an interface 500 in the pressure vessel. As another example, the heated fuel and hydrogen generating fluid may be immiscible and may be separated by a pressure vessel interface 500. Although not required, the interface 500 can be formed from a fluid interface between the heated fuel and hydrogen generating fluid interface layers in the pressure vessel 459. As a further example, the heated fuel and hydrogen generating fluid may be separated by a physical or structural separation member, such as a pressure transfer section as described below that forms the interface 500.

  The pressure vessel may be described as a fuel vessel, a fuel cartridge, or a feedstock vessel or cartridge. As described in further detail herein, in some embodiments, the pressure vessel may be described as a dual fuel or composite fuel feed vessel or cartridge. Although illustrated with a single pressure vessel and a single valve assembly, the feed transport system 22 may include multiple pressure vessels and / or multiple valve assemblies within the scope of the present disclosure. In addition, the plurality of pressure vessels 459 may be in fluid communication with a single valve assembly. In the example shown in FIG. 32, the fluid source (feed) stream 16 and the fuel feed stream 64 are configured to be discharged from the same pressure vessel 459 and these streams are configured by the same valve assembly 460. Be controlled. However, as described, this structure is not essential.

  32-33, the interface 500 takes the form of a structural interface in the form of a pressure transfer portion 488, which is a fluid bag 488 in the illustrated example. The pressure transmitter may alternatively be described as partitioning the internal cavity 480 into a first or pressurized chamber 495 and a second or pressurized chamber 497. The pressure transmission unit 488 may be configured to adjust the relative volumes of the first chamber 495 and the second chamber 497 according to changes in the volume and / or pressure in these chambers. For example, the pressure transmitter can be configured to automatically move within the cavity to adjust the relative dimensions of the chamber. As a more specific example, when the amount of hydrogen generating fluid 15 decreases in chamber 495, the pressure transmitter typically decreases the size of chamber 495 in response to an increase in the size of chamber 497. Can move within the cavity to accommodate this change in the fluid 15. While the pressure transfer section may apply some pressure to the pressurized fluid itself, it is also within the scope of the disclosure that the pressure transfer section does not apply pressure (or not at all) to the pressurized fluid. The pressure transmission portion may have any suitable structure having a foldable flexible fluid bag, as shown in FIGS. 32 and 33, by way of example. For example, the pressure transmitter can be any structure configured to allow the transmitter to slide or otherwise move within the cavity, the transmitter being flexible and elastically deformable. It may include a structure that is rigid but can be scaled as described above.

  As described above, the heated fuel 13 may be referred to as a pressurized fuel when used to pressurize and propel the hydrogen generating fluid. Correspondingly, the hydrogen generating fluid 15 may be referred to as pressurized fuel or fluid. When heated fuel is placed in the pressure vessel, this fuel is stored under its own pressure which is sufficient to apply pressure to the hydrogen generating fluid 15. The pressurized heated fuel 13 can be selected to be present in the vessel 459 as a two-phase system including a liquid phase and a vapor phase. This allows the pressure vessel to maintain a constant or substantially constant pressure on the hydrogen generating fluid 15, especially when the temperature of the pressure vessel remains constant. For example, the heated fuel can be selected to be in vapor-liquid equilibrium when the feed transport system 22 is set to hydrogen production. An example of the two-phase pressurized fuel 13 is shown in FIG. 34, in which the liquid phase is indicated by 501 and the gas phase is indicated by 503. As the hydrogen generating fluid 15 or the heated fuel 13 is released from the pressure vessel 459, a part of the heated fuel 13 in the liquid phase evaporates into the vapor phase. Then, the empty space of the internal cavity 480 is filled. Accordingly, even when the heated fuel or hydrogen generating fluid is being released, the heated fuel 13 applies a substantially constant pressure to the hydrogen generating fluid 15. While it is within the scope of the present disclosure to utilize any of the heated fuels described herein, propane is a suitable additive for use in a feed transport system having a pressure vessel according to the present disclosure. Pressure fuel.

  FIG. 34 shows another example of a pressure vessel 459 that can be used in the feed transport system of the present disclosure. Similar to the pressure vessel shown in FIGS. 32 and 33, the pressure vessel shown in FIG. 34 receives the heated fuel 13 and the hydrogen generating fluid 15 and is at least substantially at the interface 100 separating the fuel and fluid. Define internal cavities 80 that are kept separate from each other. Similarly, one of fuel 13 and fluid 15 may be pressurized fuel or fluid, and the other may be pressurized with pressurized fuel / fluid. However, unlike the example shown in FIGS. 32 and 33, the interface between fuel and fluid in FIG. 34 does not include a structural barrier or surface that divides the cavity 480 into sections 495 and 497. Instead, FIG. 34 shows that the interface can be formed by the nature of the heated fuel and the hydrogen generating fluid. As described, even in the absence of structural barriers between fluids, immiscible fluids can be maintained at least substantially separately, if not completely. Similarly, if one of the fuel 13 and fluid 15 is a gas and the other is a liquid, the fuel and fluid are kept at least substantially separate by an identifiable interface formed again therebetween. It can be drunk.

  FIG. 34 also shows the length of the fluid conduit 520 that extends into the internal cavity 480 to establish fluid communication with the fluid at the end of the discharge orifice 490 of the container. Alternatively, the pressure vessel may include a discharge orifice in a cavity region that contains a specific one of fuel 13 or fluid 15. As yet another example, a fluid conduit may be used that extends through the wall or body of the pressure vessel at the inlet in the corresponding region of the pressure vessel where the fluid / fuel is located. The heated fuel 13 and the hydrogen generating fluid 15 are shown by a solid line and a dotted line in FIG. 34, and the relative positions of these members in the pressure vessel and / or the pressurized / pressurized relationship disclosed herein are all. It is visually fixed that it may vary based on the specific application of the pressure vessel, the mechanism used to generate hydrogen gas, the composition of the fuel and / or fluid, etc. Show. Suitable elements of the non-limiting example shown include the use of propane or other liquefied gas as the pressurized heated fuel, methanol, methanol and water, or other alcohols as the pressurized hydrogen generating fluid, or Using an alcohol-water mixture.

  In FIG. 33, pressure vessel 459 is shown including a discharge orifice 490 defined by pressure vessel discharge region 492. The position of the orifice 490 and the shape and orientation of the container 459 can vary within the scope of the present disclosure. Although the discharge orifice 490 is illustrated as being closed by a closure member 494 having first and second flow paths 496 and 498 defined therein, any suitable structure and / or configuration is described herein. Within the scope of this disclosure. The closure member may include any device or arrangement of devices configured to seal a discharge orifice other than the flow through the flow path or outlet defined by the closure member. Separate and discrete first and second flow paths 496 and 498 are configured to reduce or eliminate the cross-sectional area of the discharge stream from which the one or more feed streams described above are created. However, it is within the scope of the disclosure that the flow path includes a common fluid conduit that selectively flows the fuel 13 and fluid 15, depending on the configuration of the valve assembly 460. Sealant, gaskets, and other such equipment are not only in the pressure vessel, but also to help maintain a separation between fuel 13 and fluid 15 as they are released. 22 may be included.

  FIG. 33 provides a graphical illustration in which the pressure vessel can include a plurality of discharge orifices, with the pressure vessel of FIG. 33 including first and second discharge regions 492 and 493. The first and second discharge regions are first and second discharge orifices through which heated fuel and hydrogen generating fluid are selectively discharged at the outlets or flow paths 496 and 498 (depending on the valve assembly settings). 490 and 491, respectively. FIG. 33 shows an example of a valve assembly 460 that includes valves 461 and 463 and also visually illustrates a feed transport system that is configured to transport the heated fuel 13 and the hydrogen generating fluid 15 to the fuel processing system 31. To express.

  As described, the valve assembly 460 is configured to control or discharge the flow of heated fuel and hydrogen generating fluid from the pressure vessel. Valve assembly 460 includes at least one valve and may include any suitable structure for selectively regulating flow flow from a pressure vessel. 30 and 32 are schematic views of the valve assembly 460 such that the components of the valve assembly can be integrated with the pressure vessel, attached directly to the pressure vessel, and / or downstream from the pressure vessel and the hydrogen generation region and heating. It is intended to visually show that it can be in fluid communication with the pressure vessel, such as connected upstream from the assembly. In other words, the valve assembly 460 may be configured as part of the pressure vessel 459 or may be separate from the pressure vessel but still in fluid communication with the heated fuel and hydrogen generating fluid.

  The valve assembly 460 is configured to selectively and separately release the hydrogen generating fluid and the heated fuel from the pressure vessel 459. For example, the valve assembly 460 may be configured to allow selective release of the heated fuel and hydrogen generating fluid, but configured not to allow the heated fuel and hydrogen generating fluid to be released as a single stream. Can be done. In some embodiments, this release of the hydrogen generating fluid may be under pressure as applied by the heated fuel. It is within the scope of the present disclosure that the relationship may be reversed for heated fuel being released under the pressure applied by the hydrogen generating fluid.

  The valve and / or valve assembly may be configured to simply allow or restrict the corresponding flow rate through certain orifice dimensions. It is understood that the valve and / or valve assembly may be configured to adjust or change the flow rate of any or any flow, such as adjusting the relative size of the orifice through which the flow passes through the valve assembly. It is also within the scope of the disclosure. It is within the scope of the present disclosure that the valve assembly can operate between a flow present and no flow setting and / or via any suitable mechanism, such as to adjust the relative proportions of flow. But there is. The examples shown are for example predetermined trigger events such as being manually activated by an individual in the vicinity of the valve assembly, activated by a controller or other electronic device or signal, or detected temperature, pressure, flow conditions, etc. A valve assembly configured to operate automatically in response to detection or occurrence.

  As visually illustrated in FIG. 35, valve assembly 460 includes a first valve 461 configured to release heated fuel and a second valve configured to discharge hydrogen generating fluid. A valve 463 may be included. Valve assembly 460 may additionally or alternatively include a three-way valve. The three-way valve can be configured to selectively allow the release of heated fuel, allow the release of hydrogen product fluid, or prevent the release of heated fuel and hydrogen product fluid. The three-way valve has an off setting that does not allow discharge of fluid from the pressure vessel, a heating setting that allows discharge of heated fuel from the pressure vessel, and a hydrogen generation setting that allows discharge of hydrogen generating fluid from the pressure vessel. Can be considered. The three-way valve can be configured to allow only the selection of the heating setting from the off configuration so that the valve passes the heating setting before selecting the hydrogen production setting. Alternatively, the three-way valve can be configured to allow selection of any remaining setting from any selected setting.

  The three-way valve or other embodiment valve assembly 460 may be configured to allow or allow the release of heated fuel until a predetermined condition is met before allowing or allowing the release of hydrogen generating fluid. . The predetermined state may include passage of a predetermined amount of elapsed time from the start of the heating setting. In embodiments in which the feed transport system supplies heated fuel to a heating assembly in the hydrogen generation assembly, the predetermined condition may include a hydrogen generation assembly that has reached a predetermined operating temperature. The valve assembly 60 may be configured to allow selection of hydrogen production settings under the occurrence of this type of predetermined situation.

  This type of three-way valve (or other embodiment of valve assembly 60) allows selection of the heating setting from the off setting, but the selection of the hydrogen production setting until a predetermined condition occurs or is otherwise detected. A control mechanism may be included. In this state, the control mechanism is opened and the selection of the hydrogen generation setting is allowed. The valve assembly can be configured to automatically switch to a hydrogen production setting, allowing selection of a heating setting when a predetermined condition occurs or is otherwise detected. It is also within the scope of the present disclosure that a valve assembly is used that does not restrict the flow of both fuel 13 and fluid 15 simultaneously.

  Addition of a suitable feed transport system 22 that includes a pressure vessel 459 containing heated fuel 13 and hydrogen generating fluid 15 in a pressurized and pressurized relationship and that can be used in a hydrogen generating assembly in accordance with the present disclosure. A typical example is in US Provisional Application No. 60 / 623,259, filed Oct. 29, 2004, under the name “Feedstock Delivery Systems, Fuel Processing Systems, and Hydrogen Generation Assemblies Including the Same”. The full disclosure of which is hereby incorporated by reference. Additional other examples are disclosed in US patent application Ser. No. 11 / 096,827, the full disclosure of which can be incorporated herein by reference.

  Similar to the hydrogen generation assembly 10 schematically illustrated in FIG. 30, the hydrogen generation assembly 10 in FIG. 35 includes a feed transport system 22 and a fuel processing system 31. In one example, the feed transport system 22 includes a pressurized source 499 of heated fuel 13 and hydrogen generating fluid 15 in the form of a pressure vessel 459. As shown, pressure vessel 459 includes an internal compartment or cavity 480 that contains both heated fuel 13 and hydrogen generating fluid 15 and a valve assembly 460 that allows separate flow of fuel 13 and fluid 15. As shown, valve assembly 460 includes first and second valves 461 and 463. However, the valve assembly 461 can be configured according to any of the variations described herein, including the use of a three-way valve. The feed transport system 22 illustrated also in FIG. 35 includes first and second discharge orifices 490 and 491. The first and second flow paths 496 and 498 are illustrated in FIG. 35 as extending from the first and second discharge orifices 490 and 491 to the fuel processing system 31.

  The pressure vessel 459 is disposed in the hydrogen generating fluid 15 disposed in the fluid bag, the heated fuel 13 disposed in the internal cavity 480 of the pressure vessel that surrounds and pressurizes the fluid bag 486, and the inside. Any or other described, illustrated, and / or incorporated in this application as shown in FIG. 35 as including a pressure transfer portion 488 configured as a fluid bag 486 having a hydrogen generating fluid 15 to be The pressurized source and / or pressure vessel can be used in place of the pressure vessel 459 shown in FIG.

  An example of the hydrogen generating fuel cell system 42, the hydrogen generating fuel processing assembly 10 and the feed transport system 22 is illustrated in schematic form herein. These systems are not essential, but include additional air / oxidant supply and transport systems, heat exchange assemblies and / or sources, controllers, sensors, valves, and other flow controllers, power control modules, etc. A member may be included. It is within the scope of the present disclosure that one or more of these members can be selectively included. Similarly, although a single fuel processor 12 and / or a single fuel cell stack 40 is shown in the drawings, it is within the scope of the disclosure that any or both of these members can be used. .

[Industrial applicability]
The present disclosure can be applied to the fields of hydrogen production, feed transport and power generation.

  The disclosure disclosed above is believed to include a number of different inventions with independent utility. Although each of the inventions is disclosed in its preferred form, the specific embodiments of the invention disclosed and shown herein are not to be considered as limiting. This is because many variations are possible. The subject matter of the present invention includes all novel and non-obvious combinations and sub-combinations of the various elements, features, functions and / or properties disclosed herein. Similarly, when a claim refers to a “one” or “first” element or a similar description, such a claim may contain one or more such elements. It must be understood as possible. And two or more such elements are not essential nor are they excluded.

  Each claim is directed to a specific combination and sub-combination that is new and non-obvious for one of the disclosed inventions. Inventions implemented in other combinations and sub-combinations of such features, functions, elements and / or characteristics may be recited in the claims by this or a related application as amendments to the current claims or as new claims. Such amended or new claims, whether directed to different inventions or to the same invention, differ from the scope of the original claims, become wider or narrower. Whether or not identical, are considered to be within the scope of the inventive subject matter of the present disclosure.

FIG. 1 is a schematic diagram of a hydrogen generation assembly according to the present disclosure. FIG. 2 is a schematic diagram of a hydrogen generating fuel cell system according to the present disclosure. FIG. 3 is a schematic diagram of another hydrogen generating fuel cell system according to the present disclosure. FIG. 4 is a schematic diagram of another hydrogen generating fuel cell system according to the present disclosure. FIG. 5 is a schematic diagram of another hydrogen generation assembly according to the present disclosure. FIG. 6 is a schematic diagram of another hydrogen generation assembly according to the present disclosure. FIG. 7 is an exploded perspective view of an exemplary fuel processing assembly according to the present disclosure. FIG. 8 is an exploded perspective view of the fuel processing assembly of FIG. FIG. 9 is another exemplary perspective view of a fuel processing assembly according to the present disclosure. 10 is a cross-sectional perspective view of the fuel processing assembly of FIG. 11 is an exploded perspective view of the fuel processing assembly of FIG. FIG. 12 is a schematic diagram of another exemplary hydrogen generation assembly according to the present disclosure. FIG. 13 is a partial isometric view illustrating an embodiment of a burner structure that may be used in a heating assembly according to the present disclosure. FIG. 14 is an exemplary side view of a hydrogen generating fuel processing assembly according to the present disclosure. 15 is a cross-sectional view of the hydrogen generating fuel processing assembly of FIG. FIG. 16 is a side view of another exemplary hydrogen generation assembly in accordance with the present disclosure that is configured to be activated using liquid fuel. FIG. 17 is a side view of another exemplary hydrogen generation assembly in accordance with the present disclosure that is configured to be activated using liquid fuel. FIG. 18 is a side view of another exemplary hydrogen generation assembly in accordance with the present disclosure that is configured to be activated using liquid fuel. FIG. 19 is an end view of the hydrogen generation assembly of FIG. FIG. 20 is a perspective view of an exemplary hydrogen generating fuel processing assembly according to the present disclosure. FIG. 21 is another perspective view of the hydrogen generating fuel processing assembly of FIG. 22 is a partial cross-sectional view of the hydrogen generating fuel processing assembly of FIG. FIG. 23 is a partial schematic diagram of a hydrogen generation assembly having an exemplary feed transport system according to the present disclosure where both the hydrogen generation zone and the feed transport system receive the same liquid carbon-containing feed. FIG. 24 is a schematic diagram illustrating a variation of the hydrogen generation assembly of FIG. 23 with the carbon-containing feed being transported from the same feed stream to the hydrogen generation zone and burner assembly. FIG. 25 is a schematic diagram of another exemplary hydrogen generation assembly in accordance with the present disclosure, where the hydrogen generation zone and burner assembly both receive fuel or a stream containing feedstock, water and liquid carbon-containing feedstock. FIG. 26 shows a variation of the hydrogen generation assembly of FIG. 25 in which both the hydrogen generation zone and the burner assembly accept a stream containing fuel or feed, water from the same feed stream and a carbon-containing feed. FIG. FIG. 27 is a schematic diagram illustrating another variation of the hydrogen generation assembly of FIGS. FIG. 28 is a schematic diagram of a hydrogen generation assembly in another embodiment of a feed transport system according to the present disclosure. FIG. 29 is a schematic diagram of a hydrogen generation assembly in another embodiment of a feed transport system according to the present disclosure. FIG. 30 is another exemplary schematic diagram of a fuel cell system according to the present disclosure. FIG. 31 is a schematic diagram of another exemplary feed transport system according to the present disclosure. FIG. 32 is a schematic diagram of another feed transport system according to the present disclosure. FIG. 33 is a schematic diagram of another hydrogen generation assembly according to the present disclosure. FIG. 34 is a schematic diagram of another feed transport system that is disclosed herein. FIG. 35 is a schematic diagram of another hydrogen generation assembly as disclosed herein.

Explanation of symbols

DESCRIPTION OF SYMBOLS 10 Hydrogen production assembly 12 Fuel processor 11 Feed stream 13 Pressurized fuel 14 Generated hydrogen stream 15 Hydrogen production fluid 16 Feed stream 17 Water 18 Carbon-containing feed 19 Hydrogen production region 20 Output stream 22 Feed transport system 23 Steam reforming catalyst 24 Purification region 26 Hydrogen rich stream 27 Housing 28 By-product stream 30 Hydrogen selective membrane 31 Fuel processing system 32 Chemical carbon monoxide removal assembly 38 Pressure swing adsorption system 40 Fuel cell stack 44 Fuel cell 46 Energy consuming equipment 48 End plate 52 Energy storage 55 Pneumatic transport assembly 60 Heating assembly 64 Fuel stream 66 Emission stream 68 Shell 69 Evaporation zone 90 Composite feed stream 100 Pump assembly 102 Pump 106 Inlet 108 Outlet 110 Liquid stream 112 Supply (source)
116 Liquid Stream 120 Recycle Stream 130 Intake Conduit 132 Outlet Conduit 134 Transport Conduit 136 Recycle Conduit 140 Flow Restrictor 142 Orifice 144 Open 150 Pressure Actuated Valve 152 Bypass Conduit 154 Bypass Flow 158 Energizing Mechanism 230 Filter 232 Restrictor Orifice 358 Main Burner Assembly 376 Fuel chamber 378 Heat ignition source 380 Ignition zone 400 Resistive element 404 Top member 406 Baffle 407 Flame passage 408 Ignition chamber 410 Transport medium 412 Top 415 Tube 412 Pre-heating conduit 424 Structure 480 Internal cavity 488 Fluid bag 495 First chamber 497 Second chamber 499 Supply source 500 Interface (interface)

Claims (38)

A hydrogen generation assembly comprising a fuel processing assembly comprising:
The fuel processing assembly includes:
A hydrogen production region configured to receive at least a feed stream comprising at least a carbon-containing feedstock and to produce a mixed gas stream comprising hydrogen gas as a major component;
At least one purification region configured to receive the mixed gas stream and divide the mixed gas stream into at least one product hydrogen stream and at least one byproduct stream;
A heating assembly configured to combust a fuel stream to produce a heated discharge stream for heating at least the hydrogen production zone;
A flow restrictor between the hydrogen generation zone and the heating assembly;
A feed transport system configured to transport a feed stream comprising at least a carbon-containing feedstock to the hydrogen generation region of the fuel processing assembly;
The fuel processing assembly is configured to produce hydrogen gas of at least 3 slm and no more than 20 slm when operating at full capacity;
The heating assembly is configured to receive and burn the by-product stream when the hydrogen generation region is generating hydrogen gas;
The flow restrictor is configured to generate a back pressure of a fluid conduit through which the by-product stream flows to the heating assembly;
The feedstock transport system is in fluid communication with a liquid supply containing carbon-containing feedstock,
The feedstock transport system is
A pump assembly configured to withdraw a liquid inlet stream containing at least a carbon-containing feedstock from the supply to discharge a liquid outlet stream;
An outlet conduit in fluid communication with the transport conduit and the recycle conduit;
A flow restrictor configured to generate a back pressure of the recycling conduit;
A pressure actuated valve configured to allow liquid in the recycle conduit to selectively bypass the flow restrictor;
With
The transport conduit is in fluid communication with the hydrogen generation region of the hydrogen generating fuel processing assembly, and the recycling conduit is fluidly connected to at least one of the liquid supply and an inlet conduit that draws an inlet stream to the pump assembly. A hydrogen generation assembly in communication, wherein the outlet conduit is configured to receive a liquid outlet stream and define a flow path to the transport conduit and the recycling conduit for the liquid outlet stream.   The hydrogen generation assembly of claim 1, wherein the pressure-actuated valve is in fluid communication with a bypass conduit extending in fluid communication with a portion downstream of the flow restrictor and upstream of the recycle conduit. The pressure activated valve allows the pressure activated valve to restrict the flow of the liquid outlet flow through the bypass conduit, and the pressure activated valve allows the flow of the liquid outlet flow through the bypass conduit. Configured to be selectively set between the operational settings,
The pressure actuated valve is biased to the closed setting;
The hydrogen generating assembly of claim 2, wherein the pressure activated valve is configured to transition to the operational setting when a pressure of a liquid outlet stream in the transport conduit exceeds a threshold recycle pressure. The hydrogen generation region has a threshold transport pressure for the portion to which the liquid outlet stream is transported;
The threshold recycle pressure corresponds to the threshold transport pressure,
The hydrogen generation assembly of claim 3, wherein the threshold recycle pressure is less than the threshold transport pressure. The hydrogen generation region is configured to receive up to a threshold flow rate of the outlet stream via the transport conduit;
The hydrogen generation assembly according to any one of claims 1 to 4, wherein the pump assembly is configured to discharge a liquid outlet stream having a flow rate greater than the threshold flow rate. The heating assembly is in heat transfer with the hydrogen generation region;
The heating assembly includes at least one fuel chamber and at least one heating ignition source;
The at least one fuel chamber is configured to receive at least one fuel stream at a first temperature;
The at least one fuel stream includes a liquid combustible carbon-containing fuel having an ignition temperature higher than the first temperature;
The at least one heat ignition source increases the temperature of at least a portion of the carbon-containing fuel to a second temperature at least equivalent to the ignition temperature to ignite the carbon-containing fuel. 6. The hydrogen generation assembly according to any one of claims 1 to 5, wherein the hydrogen generation assembly is configured to heat at least a portion of.   The hydrogen generation assembly of claim 6, wherein the feed transport system is further configured to transport the at least one fuel stream to the at least one fuel chamber. It said fuel chamber receives a large amount of liquid combustible carbon-containing fuels, including open released container that is configured to store at least temporarily, the hydrogen generation assembly of claim 7.   The heating assembly further includes a transport medium disposed in the fuel chamber, wherein the transport medium is configured to at least temporarily absorb the liquid combustible carbon-containing fuel. Or a hydrogen generation assembly according to claim 8. The heating assembly further includes a transport medium disposed in the fuel chamber, wherein the transport medium is configured to define a flame holding surface for the fuel, the flame holding surface being the fuel. 9. A hydrogen generation assembly according to claim 7 or claim 8 configured to maintain a combustion flame at a predetermined distance from one or more members of the processing assembly . In combination with a fuel cell stack configured to generate current from an oxidant and at least a portion of the product hydrogen stream;
11. The hydrogen generation assembly according to any one of claims 1 to 10, wherein the fuel cell stack has a rated power in the range of 100-1000 watts. A hydrogen generation assembly,
A feed transport system configured to selectively transport a heated fuel and a hydrogen generating fluid;
A hydrogen generation region configured to receive the hydrogen generation fluid from the feed transport system and to generate a flow including hydrogen gas as a major component therefrom;
A heating assembly configured to receive the heated fuel from the feed transport system and to combust the heated fuel to produce a combustion discharge stream for heating at least a hydrogen generation region;
A fuel cell stack configured to receive at least a portion of the flow comprising hydrogen gas and generate current therefrom;
With
The feedstock transport system is
A valve assembly configured to selectively and individually release the hydrogen generating fluid and the heated fuel;
The valve assembly is configured to discharge the heated fuel until a predetermined state occurs before releasing the hydrogen generating fluid, and the predetermined state is a predetermined time from the start of the discharge of the heated fuel. Elapses and the hydrogen generation assembly reaches a predetermined operating temperature,
The valve assembly is configured to automatically switch between releasing the heated fuel and releasing the hydrogen generating fluid upon occurrence of the predetermined condition;
The fuel cell stack is a hydrogen generation assembly having a rated power in the range of 100-1000 watts.   The valve assembly includes a three-way valve that is selectively set to release the heated fuel, release the hydrogen generating fluid, or prevent release of the heated fuel and the hydrogen generating fluid. Item 13. The hydrogen generation assembly according to Item 12. The valve assembly is configured to automatically switch between releasing the heated fuel and releasing the hydrogen generating fluid without requiring input from a computerized controller. 14. The hydrogen generation assembly according to any one of claims 12 to 13 , wherein: A controller configured to automatically set the valve assembly between a plurality of settings;
The plurality of settings includes at least a setting in which the valve assembly is configured to release the heated fuel, and a setting in which the valve assembly is configured to discharge the hydrogen generating fluid. The hydrogen generation assembly according to any one of claims 12 to 13 . The feed transport system includes at least one pressure vessel containing heated fuel and a hydrogen generating fluid;
The heated fuel is disposed in the pressure vessel and is configured to be transported to the heating assembly under the pressure of the heated fuel itself;
The hydrogen generating fluid is placed in said pressure vessel and said heating fuel or et away septum for transporting the hydrogen-producing region at a pressure that is applied by the heating fuel,
The pressure vessel includes a first discharge orifice and a second discharge orifice;
The pressure vessel is configured to discharge the heated fuel through the first discharge orifice;
16. The hydrogen generation assembly according to any one of claims 12 to 15 , wherein the pressure vessel is configured to discharge the hydrogen generating fluid through the second discharge orifice. The heating fuel and the hydrogen generating fluid is immiscible, hydrogen generation assembly of claim 16. A pressure transmission part disposed in the pressure vessel and dividing the pressure vessel into a pressurized chamber and a pressurized chamber;
18. A hydrogen generation assembly according to claim 16 or claim 17 , wherein the heated fuel is disposed in the pressurized chamber and the hydrogen generating fluid is disposed in the pressurized chamber. The pressure vessel during operation of the hydrogen generation assembly, least greater than even 1 00Psi, and is maintained at a pressure below 250 psi, hydrogen according to claims 16 to any one of claims 18 Generate assembly. 20. The hydrogen generation assembly according to any one of claims 1 to 19 , wherein the hydrogen generation region and at least one purification region are housed in a sealed shell. A portable hydrogen generation assembly,
A fuel processing assembly having a hydrogen generation region configured to generate hydrogen gas from a feed stream comprising water and a carbon-containing feedstock;
A burner assembly configured to combust at least one fuel stream to produce a heated discharge stream for heating at least the hydrogen production region to at least a minimum hydrogen production temperature;
A housing containing at least the fuel processing assembly and the burner assembly;
A feed transport system configured to selectively transport the feed stream to the hydrogen generation zone and the fuel stream to the burner assembly;
A fuel cell stack configured to receive at least a portion of the hydrogen gas generated by the fuel processing assembly and generate current therefrom;
With
The fuel processing assembly includes a sealed shell surrounding the hydrogen generation region and at least one purification region;
The fuel cell stack has a rated power in the range of 100-1000 watts, and when operated at full capacity, the hydrogen generation region is configured to generate less than 20 slm of hydrogen gas. Generate assembly. The hydrogen generation assembly of claim 21 , wherein the assembly is configured to begin the initial generation of hydrogen gas without the need for a computerized controller. 23. The hydrogen generation assembly of claim 21 or claim 22 , wherein the feed transport system is configured to transport the feed stream and the fuel stream without utilizing a mechanical pump. The hydrogen-producing region, when operating at full capacity, is configured to produce hydrogen of less than 10 slm, and the fuel cell stack, Ru have a rated output 600 W or less, according claim 1 Item 24. The hydrogen generation assembly according to any one of Items 23 . 25. A method according to any one of claims 1 to 24 , wherein the feed stream comprises water and a carbon-containing feed. Each of said feed stream and the fuel stream, including at least one common carbon-containing component, the hydrogen generation assembly according to any one of claims 25 to claim 1. Each of said feed stream and said fuel stream comprises at least 25% by volume of water and at least one water-soluble carbon containing component, hydrogen generation assembly according to any one of claims 26 claim 1. The hydrogen generation region includes a steam reforming catalyst,
The hydrogen-producing region is adapted to produce a mixed gas stream containing hydrogen gas and other gases, the hydrogen gas forms a major component of the mixed gas stream, wherein from claim 1 to claim 27 A hydrogen generation assembly according to any one of the preceding claims. Wherein at least one purification region, including the region containing at least one hydrogen-selective membrane, the hydrogen generation assembly according to any one of claims 28 claim 1. A hydrogen generation region configured to receive at least one feed stream having a minimum hydrogen production temperature and including at least a carbon-containing feedstock and to generate an output stream including hydrogen gas as a major component; A method of activating and operating the hydrogen generation assembly in a hydrogen generation assembly comprising:
Transporting at least one fuel stream comprising a liquid combustible carbon-containing fuel to a heating assembly at a first temperature;
Heating the fuel stream in the heating assembly to a second temperature at least equivalent to an ignition temperature with at least one heating and ignition source;
Igniting the fuel stream in the heating assembly with the at least one heat ignition source to generate a combustion stream;
Heating the hydrogen generation zone of the hydrogen generation assembly with the combustion stream to a predetermined temperature associated with the minimum hydrogen generation temperature of the hydrogen generation zone;
Drawing a liquid feed stream from a feed comprising at least one carbon-containing feed to the hydrogen production zone of the hydrogen producing fuel cell system;
Pumping the liquid feed stream stream through an outlet conduit in fluid communication with a first portion of a transport conduit and a recycle conduit;
Adjusting the distribution of the flow between the transport conduit and the recycling conduit;
Receiving at least a portion of the flow in the hydrogen generation region and providing the output stream comprising hydrogen gas therefrom;
Including
The carbon-containing fuel has an ignition temperature higher than the first temperature;
The transport conduit is in fluid communication with the hydrogen generation region of the hydrogen generation assembly, and the recycle conduit is for returning the liquid feed stream to at least one of the upstream location from the supply and transport mechanism. Configured to provide a flow path;
The transport mechanism is configured to propel the liquid flow to the outlet conduit;
The pumping step provides a liquid flow stream that exceeds the capacity of the transport conduit, with an excess portion of the flow flowing to the recycle conduit;
The adjusting includes generating a back pressure in the recycling conduit with a flow restrictor;
The flow restrictor at least separates the recycling conduit into a first portion extending between the outlet conduit and the flow restrictor and a second portion extending from the flow restrictor. And
The conditioning comprises an excess portion of the flow for bypassing from the flow restrictor by flowing through a bypass conduit upstream of the recycle conduit and in fluid communication with a portion downstream of the flow restrictor. The method further comprises selectively allowing. 31. The method of claim 30 , comprising automatically adjusting a flow distribution between the transport conduit and the recycle conduit. 31. The method of claim 30 , wherein the selectively allowing includes restricting the liquid flow through the bypass conduit until the flow pressure exceeds a threshold recycle pressure. 33. The method of claim 32 , wherein the threshold recycle pressure is less than a threshold transport pressure for the portion of the stream that is transported to the hydrogen production region. The selectively allowing is allowing the flow of the liquid stream through the bypass conduit until at least the pressure of the flow is less than the threshold recycle pressure, and then via the bypass conduit. The method of claim 32 , comprising restricting the flow of the liquid feed stream. The selectively allowing is
Utilizing a pressure-actuated valve configured to be selectively set between a closed setting and an operational setting;
The closed setting is such that the pressure activated valve restricts flow through the bypass conduit;
The operating setting is such that the pressure-actuated valve allows excessive flow through the bypass conduit;
The pressure actuated valve is biased to the closed setting;
32. The method of claim 30 , wherein the pressure activated valve is configured to transition to the operational setting when the flow pressure exceeds a threshold recycle pressure. 36. A method according to any one of claims 30 to 35 , wherein the liquid stream comprises water and a carbon-containing feedstock. 37. A method according to any one of claims 30 to 36 , wherein each of the feed stream and the fuel stream comprises at least one common carbon-containing component transported from a common feed. 38. A method according to any one of claims 30 to 37 , wherein each of the feed stream and the fuel stream comprises at least 25% by volume water and at least one water soluble carbon-containing component.

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